JP2017128686A - Compound manufacturing system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a compound manufacturing system capable of making a compound that can delay the depletion of fossil fuel by reducing the use amount of fossil fuel.SOLUTION: The compound manufacturing system 10A is formed of: a pure water producing apparatus 11 for producing pure water by purifying water water-supplied from a water source; a hydrogenation treatment apparatus 12 for producing hydrogen ion water from pure water by using dravite porous ceramics; a hydrogen gas first generating apparatus 13 for producing high concentration hydrogen ion water by electrolyzing the hydrogen ion water and generating hydrogen gas; a minus power source generating apparatus 14 for producing high concentration hydrogen ion water from which plus charges are removed by applying minus electricity to the high concentration hydrogen ion water; and a stirring and mixing apparatus 16 for adding a fossil fuel to the high concentration hydrogen ion water from which plus charges have been removed and mixing and stirring the high concentration hydrogen ion water and the fossil fuel, and for making a compound by electron-coupling the high concentration hydrogen ion water and the fossil fuel.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a compound production system for producing a compound used as a fuel for an internal combustion engine.

Hydrogen raw material oil consisting of a mixture of oxygenated hydrocarbon compounds and sulfur-containing hydrocarbon compounds derived from animal and vegetable oils or fats, or a mixture of petroleum-based base materials obtained by further refining crude oil in the mixed oil A fuel oil base material obtained by performing a chemical conversion treatment is disclosed (see Patent Document 1). In the hydrotreatment, in the presence of hydrogen, a support made of a porous inorganic oxide containing two or more elements selected from aluminum, silicon, zirconium, boron, titanium, and magnesium is added to the periodic table groups 6A and 8A. A catalyst supporting one or more metals selected from group elements is used. The raw material oil is hydrotreated under the conditions of a hydrogen pressure of 2 to 13 MPa, a liquid space velocity of 0.1 to 3.0 h ⁻¹ , a hydrogen / oil ratio of 150 to 1500 NL / L, and a reaction temperature of 150 to 480 ° C. The technique disclosed in Patent Document 1 can provide a fuel oil base material having excellent combustibility and oxidation stability, and having excellent life cycle characteristics from carbon neutral characteristics.

JP 2010-121071 A

  In internal combustion engines such as boilers, generators, and engines, fuels (fossil fuels) such as light oil, kerosene, and heavy oil are used as the fuel. It is a power source. However, air contains about 79% nitrogen and about 21% oxygen but contains almost no hydrogen. Furthermore, since the fuel hydrocarbons require time for molecular decomposition, the fuel combustion efficiency is 35 to 48. In addition to low combustion efficiency, its depletion by continuing to use fuel is also a problem. Also, a large amount of soot (air pollutants) containing dust, soot, sulfurous acid gas, carbon monoxide, etc. is generated during fuel combustion, causing air pollution and removing soot during fuel combustion in internal combustion engines Equipment such as filters and catalysts is required, and the unit price per unit amount of fuel cannot be lowered.

  An object of the present invention is to provide a compound production system capable of improving the combustion efficiency of fuel and making a compound capable of reducing the amount of fuel used and delaying fuel depletion. Another object of the present invention is to provide a compound production system capable of producing a compound capable of suppressing the generation of smoke (air pollutant) and preventing air pollution. Furthermore, it is providing the compound manufacturing system which can make the compound with a low unit price per unit quantity.

  The premise of the present invention for solving the above problems is a compound production system for producing a compound used as a fuel for an internal combustion engine.

  The feature of the present invention based on the above premise is that a compound production system purifies water supplied from a predetermined water source to produce pure water, and pure water purified by the pure water generator. Hydrogen gas first generator that generates hydrogen gas by electrolysis and generates high-concentration hydrogen ion water in which hydrogen ions are dissolved from pure water, and high-concentration hydrogen ion water generated by the hydrogen gas first generator Negative electricity that generates high-concentration hydrogen ion water from which positive charges are removed by energizing negative electricity and combining the negative charges of negative electricity with positive charges contained in high-concentration hydrogen ion water to remove the positive charges. A predetermined fuel is added to the high-concentration hydrogen ion water from which the positive charge has been removed by the power source generator and the negative power source generator, and the high-concentration hydrogen ion water and the fuel are mixed and stirred to obtain a high-concentration hydrogen ion water. The hydrogen ion water and the fuel in that it is formed from the stirring and mixing apparatus for making a compound with the electron coupling.

  As an example of the present invention, in the compound production system, at least two or more hydrogen gas first generators are connected in series in a state where they are arranged on the upstream side and the downstream side, and at least two or more negative power source generators are provided. They are connected in series with being arranged on the upstream side and the downstream side.

  As another example of the present invention, the first hydrogen gas generator includes a plurality of mesh electrodes having a predetermined area made of a titanium alloy and a plurality of mesh electrodes having a predetermined area made of an iridium oxide alloy. Using any one of an electrode and a plurality of mesh-like electrodes made of carbon nanotubes and having a predetermined area, the pure is electrolyzed by passing a current through the purified water.

  As another example of the present invention, the compound production system is installed between the first hydrogen gas generator and the negative power source generator or on the downstream side of the negative power source generator. A magnetic treatment device that performs magnetic treatment to remove oxygen ions dissolved in ion water and generates high-concentration hydrogen ion water from which oxygen ions have been removed; and between the hydrogen gas first generator and the negative power source generator, or An ion exchange filter device installed on the downstream side of the negative power source generator and having an ion exchange filter for removing oxygen ions dissolved in the high concentration hydrogen ion water, and generating high concentration hydrogen ion water from which oxygen ions have been removed And at least one of the above.

  As another example of the present invention, in the compound production system, at least two or more magnetic processing apparatuses are connected in series in a state of being arranged on the upstream side and the downstream side, and at least two or more ion exchange filter apparatuses are upstream. They are connected in series with being arranged on the side and downstream side.

  As another example of the present invention, the compound production system is installed on the downstream side of the negative power source generator, extracts a part of the high concentration hydrogen ion water flowing out from the negative power source generator, A hydrogen gas second generator that generates hydrogen gas by electrolyzing ionic water to generate mist-like high-concentration hydrogen ion water in which hydrogen ions are dissolved. In the compound production system, the hydrogen gas second generator The generated mist-like high-concentration hydrogen ion water is supplied to pure water.

  As another example of the present invention, the compound production system is installed on the downstream side of the magnetic processing device or the ion exchange filter device, and extracts a part of the high concentration hydrogen ion water flowing out from the magnetic processing device or the ion exchange filter device. In addition, the compound production system includes a hydrogen gas second generator that generates a mist-like high-concentration hydrogen ion water in which hydrogen ions are dissolved by electrolyzing a part of the high-concentration hydrogen ion water. Then, mist-like high-concentration hydrogen ion water generated by the second hydrogen gas generator is supplied to pure water.

  As another example of the present invention, the second hydrogen gas generator includes a plurality of mesh-shaped electrodes having a predetermined area made of a titanium alloy, and a plurality of mesh-shaped electrodes having a predetermined area made of an iridium oxide alloy. Electrolyze the high-concentration hydrogen ion water by applying current to some of the high-concentration hydrogen ion water using one of the electrodes and a plurality of mesh-shaped electrodes made of carbon nanotubes and having a predetermined area. .

  As another example of the present invention, the compound production system is installed on the upstream side of the first hydrogen gas generator, and purified water purified by a pure water generator using a mineral mainly composed of magnesium. A hydrogenation apparatus for generating hydrogen ion water in which hydrogen ions are generated and hydrogen ion water is dissolved.

  As another example of the present invention, in the compound production system, at least two or more hydrogenation processing apparatuses are connected in series in a state of being arranged on the upstream side and the downstream side.

  As another example of the present invention, the mineral is drabite porous ceramic, and in the hydrotreating apparatus, a plurality of drabite porous ceramics are accommodated, and pure water flows through these drabite porous ceramics, Hydrogen ion water in which hydrogen ions are dissolved is generated.

  As another example of the present invention, in a stirring and mixing apparatus, high-concentration hydrogen ion water and fuel are stirred and mixed while being pressurized to a predetermined pressure.

  As another example of the present invention, the oxidation-reduction potential of high-concentration hydrogen ion water is −750 mv or less.

  As another example of the present invention, the fuel is light oil, and in the compound production system, the ratio of light oil to be added to the stirring and mixing device is 60 to 70 with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring and mixing device. It is in the range of weight percent.

  As another example of the present invention, the fuel is kerosene, and in the compound production system, the ratio of kerosene to be added to the stirring and mixing device is 50 to 70 with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring and mixing device. It is in the range of weight percent.

  As another example of the present invention, the fuel is heavy oil, and in the compound production system, the ratio of the heavy oil charged into the stirring and mixing apparatus is 50 to 100% by weight with respect to 100% by weight of high-concentration hydrogen ion water flowing into the stirring and mixing apparatus. It is in the range of 70% by weight.

  As another example of the present invention, the water source is at least one of a well, rain, a river, a lake, and a pond, and the water is at least one of well water, rain storage water, river water, lake water, and pond water. One.

  The compound production system according to the present invention purifies water supplied from a predetermined water source, electrolyzes pure water to generate hydrogen gas, and high-concentration hydrogen ion water in which hydrogen ions are dissolved from pure water. The high-concentration hydrogen ion water is energized with negative electricity to generate high-concentration hydrogen ion water from which positive charges have been removed, and a predetermined fuel is added to the high-concentration hydrogen ion water from which positive charges have been removed. High-concentration hydrogen ion water and fuel are mixed and stirred, and the high-concentration hydrogen ion water and fuel are electronically coupled to form a compound. A large amount of hydrogen ions are dissolved in the compound, and hydrogen burns with the fuel during combustion. Therefore, it is possible to produce a compound that can greatly improve the combustion efficiency as compared with the case of burning only the fuel. In the compound production system, the compound produced thereby is an electronic combination of fuel and highly concentrated hydrogen ionized water. Can be reduced and fuel depletion can be delayed. Since the compound production system burns hydrogen that does not generate soot with fuel, it can produce a compound with significantly reduced soot generation compared to burning only fuel, preventing air pollution during combustion Possible compounds can be made. The compound production system can produce a compound that suppresses soot generation, so it does not require equipment such as a filter or catalyst that removes soot during combustion in internal combustion engines such as boilers, generators, engines, etc., and the unit price is low A compound can be made.

  A state in which at least two or more hydrogen gas first generators are connected in series in a state where they are arranged on the upstream side and the downstream side, and at least two negative power generators are arranged on the upstream side and the downstream side The compound production system connected in series with each other uses at least two or more hydrogen gas first generators to generate a large amount of hydrogen gas from pure to reliably generate high-concentration hydrogen ion water. By using at least two negative power supply generators, high-concentration hydrogen ionized water from which positive charges are removed can be generated. The compound production system can make a compound containing a large amount of hydrogen ions that burn with fuel, and can make a compound that can greatly improve the combustion efficiency.

  The hydrogen gas first generator has a predetermined area made of a carbon-nanotube and a plurality of mesh-shaped electrodes having a predetermined area made of a titanium alloy, a plurality of mesh-shaped electrodes having a predetermined area made of an iridium oxide alloy A compound production system that electrolyzes pure water by applying current to pure water purified by a pure water generator using any one of a plurality of mesh-like electrodes having a hydrogen gas 1 By using any of those electrodes that can improve the electrolysis capability of the generator, pure hydrogen can be reliably electrolyzed to generate a large amount of hydrogen gas. In addition to making high-concentration hydrogen ion water in which is dissolved, a compound containing a large amount of hydrogen ions can be made.

  A magnetic treatment is performed between the first hydrogen gas generator and the negative power generator or downstream of the negative power generator to remove oxygen ions dissolved in the high-concentration hydrogen ion water by the magnetic force of the permanent magnet. A compound manufacturing system including at least one of a magnetic treatment device and an ion exchange filter device having an ion exchange filter that removes oxygen ions dissolved in high-concentration hydrogen ion water is converted into high-concentration hydrogen ion water by a magnetic treatment device. By applying magnetic treatment, high-concentration hydrogen ion water from which oxygen ions (dissolved oxygen) have been removed can be made. Therefore, high-concentration hydrogen ion water from which a large amount of hydrogen ions from which oxygen ions have been removed can be made. And a compound containing a large amount of hydrogen ions can be produced. Since the compound production system can produce high-concentration hydrogen ion water from which oxygen ions (dissolved oxygen) have been removed by an ion exchange filter device, high-concentration hydrogen ion water from which a large amount of hydrogen ions from which oxygen ions have been removed is dissolved. It is possible to make a compound containing a large amount of hydrogen ions.

  At least two or more magnetic processing devices are connected in series with the upstream and downstream sides arranged in series, and at least two or more ion exchange filter devices are arranged in series with the upstream and downstream sides arranged in series. The connected compound production system uses high-concentration hydrogen ion water to magnetically treat at least two or more magnetic processing devices, thereby ensuring oxygen ions (dissolved oxygen) contained in the high concentration hydrogen ion water. Therefore, highly concentrated hydrogen ion water in which a large amount of hydrogen ions from which oxygen ions are removed can be dissolved, and a compound containing a large amount of hydrogen ions can be formed. The compound production system can make high-concentration hydrogen ion water from which oxygen ions (dissolved oxygen) are removed using at least two or more ion exchange filter devices. Dissolved high concentration hydrogen ion water can be made, and a compound containing a large amount of hydrogen ions can be made.

  A part of the high-concentration hydrogen ion water that is installed downstream of the negative power source generator and flows out of the negative power source generator is extracted, and part of the high-concentration hydrogen ion water is electrolyzed to generate hydrogen gas. Compound production including a hydrogen gas second generator that generates mist-like high-concentration hydrogen ion water in which ions are dissolved, and supplying mist-like high-concentration hydrogen ion water generated by the hydrogen gas second generator to pure water The system supplies the pure water with mist-like high-concentration hydrogen ion water obtained by further electrolyzing a part of the high-concentration hydrogen ion water by the hydrogen gas second generation device. Since the generation can be promoted, a large amount of hydrogen ions can be reliably generated in pure water in the first hydrogen gas generator, and a high concentration hydrogen ion in which a large amount of hydrogen ions are dissolved. It is possible to make a down water, can make a compound containing a large amount of hydrogen ions.

  A part of the high-concentration hydrogen ion water that is installed downstream of the magnetic treatment device or ion exchange filter device and flows out of the magnetic treatment device or ion exchange filter device is extracted, and part of the high concentration hydrogen ion water is electrolyzed. A hydrogen gas second generator for generating hydrogen gas and generating mist-like high-concentration hydrogen ion water in which hydrogen ions are dissolved, and the mist-like high-concentration hydrogen ion water generated by the hydrogen gas second generator The compound production system for supplying pure water to pure water supplies hydrogen gas by supplying mist-like high-concentration hydrogen ion water obtained by further electrolyzing part of the high-concentration hydrogen ion water to the pure water by the hydrogen gas second generator. Since the generation of hydrogen gas in the first generator can be promoted, it is possible to reliably generate a large amount of hydrogen ions in pure water in the hydrogen gas first generator. Can, it is possible to produce high concentrations of hydrogen ion water large amount of hydrogen ions are dissolved, it is possible to make a compound containing a large amount of hydrogen ions.

  The hydrogen gas second generator has a predetermined area made of carbon nanotubes and a plurality of mesh electrodes having a predetermined area made of a titanium alloy, a plurality of mesh electrodes having a predetermined area made of an iridium oxide alloy, and the like. A compound production system that electrolyzes high-concentration hydrogen ion water by applying a current to some high-concentration hydrogen ion water using any one of a plurality of mesh-like electrodes having a hydrogen gas second A mist-like high-concentration hydrogen ion water obtained by further electrolyzing a part of the extracted high-concentration hydrogen ion water by using any of those electrodes capable of improving the electrolysis ability of the generator. Since the high concentration hydrogen ion water can be supplied to pure water, generation of hydrogen gas in the hydrogen gas first generator can be promoted. In the hydrogen gas first generator, a large amount of hydrogen ions can be reliably generated in pure water, high concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved, and a compound containing a large amount of hydrogen ions. Can be made.

  Hydrogen ion is installed on the upstream side of the first hydrogen gas generator, and hydrogen is generated in the pure water purified by the pure water generator using the mineral containing magnesium as the main component. A compound production system that includes a hydrotreating device that generates hydrogen ion water in which hydrogen ions are dissolved, generates hydrogen ions in pure water using minerals containing magnesium as the main component, and generates hydrogen ion water in which hydrogen ions are dissolved. In addition, since the hydrogen ion water can be supplied to the hydrogen gas first generator, a high concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved in the hydrogen gas first generator can be easily produced. It is possible to easily produce a compound containing hydrogen ions.

  A compound production system in which at least two or more hydroprocessing apparatuses are connected in series in a state where the hydroprocessing apparatuses are arranged on the upstream side and the downstream side uses minerals by utilizing at least two or more hydroprocessing apparatuses. In hydrogenation treatment, hydrogen ions can be generated reliably in pure water to produce hydrogen ion water in which a large amount of hydrogen ions are dissolved, and high concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved in the first hydrogen gas generator. Can be made easily.

  A compound production system in which mineral is drabite porous ceramic, a plurality of drabite porous ceramics are contained, and pure water flows through these drabite porous ceramics to generate hydrogen ion water in which hydrogen ions are dissolved. By using the excellent hydrogen ion generation function of Drabite porous ceramics, hydrogen ions can be reliably generated in pure water in hydroprocessing using these minerals, and hydrogen ion water in which a large amount of hydrogen ions are dissolved. A compound containing a large amount of hydrogen ions can be produced.

  In the stirring and mixing device, the compound production system that stirs and mixes the high-concentration hydrogen ion water and the fuel in a state of being pressurized to a predetermined pressure, and applies the predetermined pressure to the high-concentration hydrogen ion water and the fuel in the stirring and mixing device. By stirring and mixing under pressure, the high-concentration hydrogen ion water and the fuel can be electronically coupled quickly and reliably, and a compound containing a large amount of hydrogen ions can be produced in a short time.

  The compound production system having a high-concentration hydrogen ion water oxidation-reduction potential of −750 mV or less is obtained by stirring and mixing the high-concentration hydrogen ion water having the redox potential and the fuel in a stirring and mixing device. And the fuel can be reliably electronically bonded, and a compound containing a large amount of hydrogen ions can be reliably produced.

  The compound production system in which the fuel is light oil and the proportion of light oil to be added to the stirring and mixing device is in the range of 60 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water flowing into the stirring and mixing device is the weight of the light oil. Since the ratio is in the range of 60 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ionized water, the amount of light oil used is greatly reduced compared to the case of burning only light oil in an internal combustion engine using light oil as fuel. (About 30 to 40% reduction), and the depletion of fuel as a raw material for light oil can be surely delayed. The compound production system burns hydrogen, which does not generate soot, together with light oil, so it can produce a compound with significantly reduced soot generation compared to the case of burning only light oil, preventing air pollution during combustion. Possible compounds can be made.

  The compound production system in which the fuel is kerosene and the proportion of kerosene charged into the stirring and mixing device is in the range of 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water flowing into the stirring and mixing device is the weight of kerosene. Since the ratio is in the range of 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ionized water, the amount of kerosene used is greatly reduced compared to burning only kerosene in an internal combustion engine that uses kerosene as fuel. (About 30 to 50% reduction), and the depletion of fuel as a raw material for kerosene can be surely delayed. Since the compound production system burns hydrogen that does not generate soot with kerosene, it can produce a compound with significantly reduced soot generation compared to burning only kerosene and prevent air pollution during combustion. Possible compounds can be made.

  The compound production system in which the fuel is heavy oil and the ratio of the heavy oil charged into the stirring and mixing device is in the range of 50 to 70% by weight with respect to 100% by weight of the high-concentration hydrogen ion water flowing into the stirring and mixing device is the weight of heavy oil. Since the ratio is in the range of 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ionized water, the amount of heavy oil used is greatly reduced compared to the case of burning only heavy oil in an internal combustion engine using heavy oil as fuel. (About 30 to 50% reduction), and the depletion of fuel as a raw material for heavy oil can be surely delayed. Since the compound production system burns hydrogen that does not generate soot with heavy oil, it can produce a compound with significantly reduced soot generation compared to burning only heavy oil and prevent air pollution during combustion Possible compounds can be made.

  A compound production system in which the water source is at least one of a well, rain, a river, a lake, and a pond, and the water is at least one of a well water, a rain storage water, a river water, a lake water, and a pond water. High-concentration hydrogen ion water can be made using existing water, and high-concentration hydrogen ion water can be produced at low cost. The compound production system uses these waters that exist in nature to produce high-concentration hydrogen ion water, and the high-concentration hydrogen ion water produced using these waters and the fuel are electronically coupled to produce a large amount of hydrogen ions. Therefore, the cost for water is not required, the compound can be made at low cost, and the compound with a low unit price can be made.

The block diagram of the compound manufacturing system shown as an example. The figure which shows an example of a hydrogenation processing apparatus. The figure which shows an example of a hydrogen gas 1st generator. The figure which shows an example of a minus electric conduction device The figure which shows an example of a hydrogen gas 2nd generator. The figure which shows an example of a stirring and mixing apparatus. The block diagram of the compound manufacturing system of FIG. 1 shown in an operating state. The block diagram of the compound manufacturing system shown as another example. The figure which shows an example of a magnetic processing apparatus. The figure which shows an example of an ion exchange filter apparatus. The block diagram of the compound manufacturing system of FIG. 8 shown in an operating state.

  The details of the compound production system according to the present invention will be described below with reference to the accompanying drawings such as FIG. 1 which is a configuration diagram of a compound production system 10A shown as an example. FIG. 2 is a diagram illustrating an example of the hydrogenation processing device 12, and FIG. 3 is a diagram illustrating an example of the hydrogen gas first generation device 13. FIG. 4 is a diagram illustrating an example of the minus electric current supply devices 30 a to 30 c, and FIG. 5 is a diagram illustrating an example of the hydrogen gas second generator 15. FIG. 6 is a diagram illustrating an example of the stirring and mixing device 16.

  The compound production system 10A includes a pure water generation device 11, a hydrotreating device 12 (mineral decomposition device), a hydrogen gas first generation device 13 (first electrolysis device), a negative power supply generation device 14, and a hydrogen gas second generation device. 15 (second electrolysis device), a stirring and mixing device 16, and an oil supply device 17. A fuel storage tank 18 or an internal combustion engine 19 such as a boiler, a generator, or an engine is connected to the compound manufacturing system 10A. The compound manufacturing system 10A manufactures a compound to be used as a fuel for the internal combustion engine 19 by a pure water purification process, a hydrogenation process, an electrolysis process, a positive charge removal process (minus electrical energization process), and a stirring and mixing process. In the compound manufacturing system 10 </ b> A, these devices 11 to 16 are arranged in the order of the pure water generator 11 → the hydrotreating device 12 → the hydrogen gas first generator 13 → the negative power supply unit 14 → the stirring and mixing device 16.

  The pure water generator 11 purifies water supplied from a predetermined water source and supplies the pure water to the hydrogenation apparatus 12. The pure water generating device 11 is connected (connected) to the hydrotreating device 12 by a supply pipe 20a through which pure water flows. The pure water generator 11 includes a continuous regeneration type pure water generator using an activated carbon tower and an RO membrane (reverse osmosis membrane), an activated carbon filter and an RO membrane (reverse osmosis membrane), and an RO membrane (reverse osmosis) using a deminer. Membrane) A pure water generator can be used. In these pure water production | generation apparatuses 11, the pure water of about 0.1 to about 1 mS / m is made. A water supply pipe 21 connected to a water source (not shown) is connected (connected) to the pure water generator 11.

  Water sources include wells, rain, rivers, lakes, and reservoirs, and at least one of these water sources can be used. Water includes well water pumped up from wells, stored water storing rain, river water drawn from rivers, lake water drawn from lakes, pond water drawn from ponds, and at least one of these waters should be used Can do. Therefore, when one type of water is supplied from these water sources to the pure water generating device 11, a plurality of types of mixed water from these water sources may be supplied to the pure water generating device 11. In addition, a water supply can also be used as a water source, and the tap water supplied from the water supply can also be used as water.

  The hydrotreating device 12 performs a hydrotreating process for generating hydrogen ions in the pure water purified by the pure water purifying device 11 to generate hydrogen ion water in which hydrogen ions are dissolved. The hydrotreating device 12 is formed of a storage container 22 that is long in one direction having an inflow port and an outflow port, and a flow tank 23 having a predetermined volume formed inside the storage container 22. In the compound manufacturing system 10A, three first to third hydroprocessing apparatuses 12a to 12c are installed. These hydrogenation processing apparatuses 12a to 12c are arranged in the order of the first hydrogenation processing apparatus 12a → the second hydrogenation processing apparatus 12b → the third hydrogenation processing apparatus 12c. Note that one or two hydroprocessing apparatuses 12 may be installed according to the amount of hydrogen ion water produced, or four or more hydroprocessing apparatuses 12 may be installed.

  The first hydrotreating device 12a is arranged on the upstream side of the second hydrotreating device 12b, and is connected (connected) to the pure water generating device 11 by the supply pipe 20a. The supply pipe 20a is connected to the outlet of the pure water generator 11 and the inlet of the first hydrotreatment device 12a. A water supply pump 24 is installed in a supply pipe 20a extending between the pure water generator 11 and the first hydrotreating device 12a. A pressure sensor (not shown) that measures the pressure of pure water flowing through the supply pipe 20a is installed in the supply pipe 20a that extends closest to the downstream side of the water supply pump 24.

  A two-way valve 25a (solenoid valve) is installed in the supply pipe 20a extending in the immediate vicinity of the first hydrotreating device 12a. The second hydrotreating device 12b is disposed on the downstream side of the first hydrotreating device 12a, and is connected (connected) in series to the first hydrotreating device 12a by the supply pipe 20b. The supply pipe 20b is connected to the outlet of the first hydrotreating device 12a and the inlet of the second hydrotreating device 12b. The third hydrotreating device 12c is disposed on the downstream side of the second hydrotreating device 12b, and is connected (connected) in series to the second hydrotreating device 12b by the supply pipe 20c. The supply pipe 20c is connected to the outlet of the second hydroprocessing device 12b and the inlet of the third hydroprocessing device 12c.

  As shown in FIG. 2, a plurality of drabite porous ceramics 26 (minerals containing magnesium as a main component) are accommodated in the flow tanks 23 of the hydrotreating apparatuses 12 a to 12 c. The drabite porous ceramic 26 is produced by firing drabite ore powder at about 1250 ° C. and has an excellent hydrogen ion generation function. The drabite porous ceramic 26 contains magnesium as a main component and contains silicic acids such as sodium, calcium, lithium, iron, manganese, and aluminum, and metal element components such as boron and fluorine.

  In these hydrotreating apparatuses 12a to 12c, pure ions flow through the drabite porous ceramics 26 accommodated in the flow tank 23, so that hydrogen ions are generated in the pure water, and the hydrogen ions are dissolved from the pure water. Hydrogen ion water is produced. In the compound manufacturing system 10A, by using the three first to third hydrotreating apparatuses 12a to 12c, hydrogen ions are reliably generated in pure water in the hydrotreating process using the drabite porous ceramic 26 (mineral). It is possible to make hydrogen ion water in which a large amount of hydrogen ions are dissolved.

  The hydrogen gas first generator 13 generates hydrogen gas by electrolyzing the hydrogen ion water generated by the hydrotreating devices 12a to 12c, and generates high-concentration hydrogen ion water from the hydrogen ion water. As shown in FIG. 3, the first hydrogen gas generator 13 includes a storage container 27 having an inflow port and an outflow port and a long electrode container 28 having a predetermined volume formed inside the storage container 27. It is formed from a single electrode 29 (cathode and anode). In the compound manufacturing system 10A, three first to third hydrogen gas first generators 13a to 13c are installed. The first hydrogen gas generators 13 are arranged in the order of the first hydrogen gas first generator 13a → the second hydrogen gas first generator 13b → the third hydrogen gas first generator 13c. One or two hydrogen gas first generators 13 may be installed or four or more hydrogen gas first generators 13 may be installed according to the amount of high-concentration hydrogen ion water produced. .

  The first hydrogen gas first generator 13a is disposed on the downstream side of the third hydrotreating device 12c, and is connected (connected) to the third hydrotreating device 12c by a supply pipe 20d. The supply pipe 20d is connected to the outlet of the third hydrotreating device 12c and the inlet of the first hydrogen gas first generator 13a. A two-way valve 25b (solenoid valve) is installed in the supply pipe 20d. The second hydrogen gas first generator 13b is disposed on the downstream side of the first hydrogen gas first generator 13a, and is connected (connected) to the first hydrogen gas first generator 13a by a supply pipe 20e. The supply pipe 20e is connected to the outlet of the first hydrogen gas first generator 13a and the inlet of the second hydrogen gas first generator 13b. The third hydrogen gas first generator 13c is disposed on the downstream side of the second hydrogen gas first generator 13b, and is connected (connected) to the second hydrogen gas first generator 13b by a supply pipe 20f. The supply pipe 20f is connected to the outlet of the second hydrogen gas first generator 13b and the inlet of the third hydrogen gas first generator 13c.

  The electrodes 29 (cathode and anode) are accommodated in the electrode tank 28 of the hydrogen gas first generator 13 and extend from the inlet of the hydrogen gas first generator 13 toward the outlet. The electrode 29 accommodated in the electrode tank 28 is made of a mesh electrode 29 having a predetermined area made of a titanium alloy, a mesh electrode 29 having a predetermined area made of an iridium oxide alloy, and a carbon nanotube. Any one of mesh electrodes 29 having a predetermined area is used. The electrode 29 made of carbon nanotubes is preferably coated on the surface with iridium oxide. A constant voltage is applied to these electrodes 29, and a constant current (DC current) or pulse current is applied.

  In the hydrogen gas first generators 13a to 13c, hydrogen ion water flows between the electrodes 29 (between the cathode and the anode) through which the current of the hydrogen gas first generator 13 is energized, thereby hydrogenating them. Hydrogen ion water generated in the processing devices 12a to 12c is electrolyzed, a large amount of hydrogen gas is generated from these electrodes 29, and high concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved is generated. In the compound manufacturing system 10A, a large amount of hydrogen gas can be generated from hydrogen ion water (electrode) by using the three first to third hydrogen gas first generators 13a to 13c. High-concentration hydrogen ion water in which ions are dissolved can be reliably generated.

  Note that in the system 10A (including the system 10B), the hydrogenation processing apparatuses 12a to 12c may not be installed. In this case, the pure water purified by the pure water generator 11 is caused to flow into the hydrogen gas first generator 13, and the hydrogen gas first generator 13 electrolyzes the pure water to generate hydrogen gas. High concentration hydrogen ion water in which hydrogen ions are dissolved is produced from water.

  The negative power source generator 14 supplies negative electricity (minus current) to the high-concentration hydrogen ion water generated by the hydrogen gas first generator 13, and the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water. Are combined to remove the positive charge, thereby generating high-concentration hydrogen ion water from which the positive charge has been removed. In the compound manufacturing system 10A, three negative power generators 14a to 14c are installed. The first to third negative power generators 14a to 14c are arranged in the order of the first negative power generator 14a → the second negative power generator 14b → the third negative power generator 14c. One or two negative power generators 14 may be installed or four or more negative power generators 14 may be installed depending on the amount of high-concentration hydrogen ion water generated from which positive charges are removed. Good.

  The negative power source generator 14 includes first to third negative electric current supply devices 30a to 30c and first to third negative electric power supply devices 31a to 31c that supply negative electricity (negative current) to the negative electric current supply devices 30a to 30c. (For example, a klystron power supply device). As shown in FIG. 4, the negative electrical energization devices 30 a to 30 c include a storage container 32 that is long in one direction having an inlet and an outlet, an electrode tank 33 having a predetermined volume formed inside the storage container 32, and a plurality of It is formed from a single electrode 34 (cathode and anode).

  The first negative electrical energization device 30a is disposed downstream of the third hydrogen gas first generator 13a, and is connected (connected) to the third hydrogen gas first generator 13a by a supply pipe 20g. The supply pipe 20g is connected to the outlet of the third hydrogen gas first generator 13a and the inlet of the first negative electrical energizer 30a. A two-way valve 25c (electromagnetic valve) is installed in the supply pipe 20g. The second negative electrical energization device 30b is disposed on the downstream side of the first negative electrical energization device 30a, and is connected (connected) in series to the first negative electrical energization device 30a by the supply pipe 20h. The supply pipe 20h is connected to the outlet of the first minus electrical energizing device 30a and the inlet of the second minus electrical energizing device 30b. The third negative electrical energization device 30c is disposed on the downstream side of the second negative electrical energization device 30b, and is connected (connected) in series to the second negative electrical energization device 30b by the supply pipe 20i. The supply pipe 20i is connected to the outlet of the second minus electric energization device 30b and the inlet of the third minus electric energization device 30c.

  These electrodes 34 (cathodes) are accommodated in the electrode tanks 33 of the negative electrical energization devices 30a to 30c, and extend from the inlet of the negative electrical energization devices 30a to 30c toward the outlet. The electrode 34 accommodated in the electrode tank 33 includes a mesh electrode 34 having a predetermined area made of a titanium alloy, a mesh electrode 34 having a predetermined area made of an iridium oxide alloy, and a carbon nanotube. Any one of the mesh electrodes 34 having a predetermined area is used. The electrode 34 made of carbon nanotubes is preferably coated on the surface with iridium oxide. A constant voltage is applied to these electrodes 34, and constant negative electricity (minus DC current) or negative pulse electricity (pulse current) is energized.

  In these minus electricity energization devices 30a-30c, minus electricity (minus current, minus pulse current) is supplied from the first to third minus power supply devices 31a-31c, and minus electricity of the minus electricity energization devices 30a-30c is energized. When high-concentration hydrogen ion water flows between the electrodes 34 (between the cathode and the anode), negative electricity is supplied to the high-concentration hydrogen ion water, and the negative charge of negative electricity and the high-concentration hydrogen ion water are included. The positive charge is removed from the high concentration hydrogen ion water by combining with the positive charge. In the negative electrical energizers 30a to 30c, high-concentration hydrogen ion water from which positive charges have been removed is generated. In the compound manufacturing system 10A, the positive charges can be reliably removed from the high-concentration hydrogen ionized water by using the three first to third negative power generators 14a to 14c, and the positive charges are removed. High concentration hydrogen ion water can be generated reliably.

  The second hydrogen gas generator 15 extracts a part of the high-concentration hydrogen ion water from which the positive charges generated by the negative power source generators 14a to 14c are removed, and electrolyzes a part of the high-concentration hydrogen ion water. Thus, hydrogen gas is generated and mist-like high-concentration hydrogen ion water is generated. The second hydrogen gas generator 15 supplies the generated mist-like high-concentration hydrogen ion water to pure water (supply pipe 20a). As shown in FIG. 5, the second hydrogen gas generator 15 includes a storage container 35 that has an inflow port and an outflow port and is long in one direction, an electrode tank 36 having a predetermined volume formed inside the storage container 35, and a plurality of It is formed of a single electrode 37 (cathode and anode). In the compound production system 10A, one hydrogen gas second generator 15 is installed, but two or more hydrogen gas second generators 15 are provided depending on the amount of high-concentration hydrogen ion water to be supplied to pure water. It may be installed.

  The second hydrogen gas generator 15 is disposed on the downstream side of the third negative electrical energizer 30c (third negative power generator 14c), and is connected (connected) to the third negative electrical energizer 30c by the return pipe 38. And connected (connected) to the supply pipe 20 a by the forward pipe 39. The return pipe 38 is connected to the vicinity of the outlet of the third negative electrical energization device 30 c and the inlet of the hydrogen gas second generator 15. The outgoing pipe 39 is connected to the outlet of the second hydrogen gas generator 15 and the supply pipe 20 a extending upstream of the feed water pump 24. A two-way valve 25d is installed in the outgoing pipe 39 extending in the vicinity of the hydrogen gas second generator 14. The electrodes 37 (cathode and anode) are accommodated in the electrode tank 36 of the hydrogen gas second generator 15. The hydrogen gas second generator 15 accommodates a mist generator 40 that makes high-concentration hydrogen ionized water mist (mist) by ultrasonic vibration.

  The electrode 37 accommodated in the second hydrogen gas generator 15 includes a mesh electrode 37 having a predetermined area made of a titanium alloy, a mesh electrode 37 having a predetermined area made of an iridium oxide alloy, and a carbon nanotube. Any one of the mesh-shaped electrodes 37 having a predetermined area is used. A constant voltage is applied to the electrodes 37, and a constant current (DC current) or pulse current is applied. In the hydrogen gas second generator 15, high-concentration hydrogen ionized water from which positive charges have been removed is obtained by passing high-concentration hydrogen ionized water between the electrodes 37 (between the cathode and the anode) through which current is passed. The electrode 37 is further electrolyzed, a large amount of hydrogen gas is generated from the electrode 37, and high-concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved is generated. The high-concentration hydrogen ion water is mist-like ( Processed into a mist).

  The stirring and mixing device 16 includes high-concentration hydrogen ion water (high-concentration hydrogen from which positive charges have been removed) generated by the hydrotreating devices 12a to 12c, the hydrogen gas first generation devices 13a to 13c, and the negative power source generation devices 14a to 14c. A fuel is added to (ion water), high concentration hydrogen ion water and fuel are stirred and mixed, and the high concentration hydrogen ion water and fuel are electronically bonded to form a compound. As shown in FIG. 6, the stirring and mixing device 16 includes a storage tank 41 that is long in one direction, a stirring tank 42 having a predetermined volume formed inside the storage tank 41, and a paddle mixer installed at the bottom of the stirring tank 42. 43a and scraping mixer 43b, a water level sensor (not shown) for measuring the water level of a mixture (compound) of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil in the stirring tank 42, and the mixers 43a and 43b are rotated. And a motor (not shown).

  In the stirring and mixing device 16, the paddle mixer 43a of the stirring tank 42 rotates in the clockwise direction or the counterclockwise direction in the range of 2000 rotations / h to 3000 rotations / h (preferably 2500 rotations / h), The scraping mixer 43b rotates in the clockwise direction or the counterclockwise direction in the range of 2000 rotations / h to 3000 rotations / h (preferably 2500 rotations / h). The inside of the storage tank 41 is maintained at a pressure higher than the atmospheric pressure. The pressure inside the storage tank 41 is in the range of 1.5 to 15 atmospheres, preferably in the range of 2.5 to 10 atmospheres.

  The stirring and mixing device 16 is disposed on the downstream side of the third negative power supply device 31c, and is connected (connected) to the third negative power supply device 31c by the supply pipe 20j. The supply pipe 20j is connected to the outlet of the third negative power supply device 31c and the side portion 44 of the storage tank 41 of the stirring and mixing device 16 and extends from the side portion 44 of the storage tank 41 toward the bottom 45 of the storage tank 41. ing. A two-way valve 25e (electromagnetic valve) is installed in the supply pipe 20j. A circulation pipe 47 is connected to the top 46 and the low part 45 of the storage tank 41.

  A circulation pipe 47 extending to the stirring tank 42 of the stirring and mixing device 16 extends from the top 46 of the storage tank 41 toward the bottom 45 of the storage tank 41. A two-way valve 25 f (electromagnetic valve) and a circulation pump 49 are installed in a circulation pipe 48 extending from the lower portion 45 of the storage tank 41 to the outside of the storage tank 41. A circulation pipe 48 extending downstream of the circulation pump 49 has a pressure sensor (not shown) for measuring the pressure of a mixture (compound) of high-concentration hydrogen ion water flowing through the circulation pipes 47, 48 and light oil, kerosene, or heavy oil. And a three-way valve 50 (solenoid valve). An oil supply pipe 51 connected to the fuel storage tank 18 or the internal combustion engine 19 is connected to the three-way valve 50.

  The oil supply device 17 accommodates any of light oil, kerosene, and heavy oil (fossil fuel) in the interior thereof, and supplies light oil, kerosene, and heavy oil to the stirring and mixing device 16. In addition to light oil, kerosene, and heavy oil, biofuel and animal and vegetable oil can be used as fuel. Biofuels include gasoline substitute Otto engine fuel (biomass alcohol fuel), diesel oil substitute diesel engine fuel, aircraft jet fuel, and gas turbine fuel.

  The oil supply device 16 includes a constant flow device (not shown), and a constant amount of light oil, kerosene, and heavy oil (liter / h) is supplied to the stirring and mixing device 16 by the constant flow device. The oil supply device 17 is connected to the stirring and mixing device 16 by an oil supply pipe 52. The oil supply pipe 52 is connected to the outlet of the oil supply device 17 and the side portion 44 of the storage tank 41 of the stirring and mixing device 16, and extends from the side portion 44 of the storage tank 41 toward the bottom 45 of the storage tank 41. The oil supply pipe 52 is provided with a two-way valve 25g (electromagnetic valve).

  Control unit of pure water generator 11, control unit of hydrogen gas first generators 13 a to 13 c, negative power source generators 14 a to 14 c, control unit of hydrogen gas second generator 15, control unit of stirring and mixing device 16, refueling The control part of the apparatus 17, a water level sensor, each pressure sensor, the control part of these two-way valves 25a-25g, the control part of the three-way valve 50, the control part of the feed pump 24, and the control part of the circulation pump 49 are control signal lines ( It is connected to a controller (not shown) via a wired or wireless connection.

  The controller is a logical computer that includes a central processing unit, a storage device, and a storage area (such as a hard disk) and is operated by a physical OS (operating system). An input device such as a numeric keypad unit and a keyboard, and an output device such as a display, a touch panel, and a printer are connected to the controller. In the storage area of the controller, set output values of the feed water pump 24 and the circulation pump 49 (flow rates of the feed water pipe 21, the supply pipes 20a to 20j, the circulation pipes 47 and 48), and the set voltage values applied to the electrodes 29, 34 and 37 The set current value for energizing the electrodes 29, 34, and 37, the set rotation speed of the paddle mixer 43 a and scraping mixer 43 b, the set oil supply amount of light oil, kerosene, and heavy oil in the oil supply device 17, the stirring tank 42 of the stirring and mixing device 16 The set water level is stored. The output of the pumps 24 and 49, the set voltage value and the set current value, the rotation speed of the mixers 43a and 43b, the amount of oil supply, and the water level can be arbitrarily changed by the input device.

  FIG. 7 is a configuration diagram of the compound manufacturing system 10A shown in an operating state. In FIG. 7, the flow of water, pure water, hydrogen ion water, high-concentration hydrogen ion water, and compounds is indicated by arrows. In order to operate the compound manufacturing system 10A, the controller is turned on to start the controller. When the controller is activated, an initial screen is displayed on a display or touch panel connected to the controller. A system ON button and a system OFF button are displayed on the initial screen. Clicking or tapping the system OFF button turns off the controller power (the same applies to the following system OFF buttons). When the system ON button is clicked or tapped, the system operation screen is displayed on the display or touch panel. On the system operation screen, an operation start button, a system OFF button, a feed water pump output setting button, a circulation pump output setting button, a rotation speed setting button, and an oil supply amount setting button are displayed.

  When the feed water pump output setting button is clicked or tapped, the feed water pump output setting screen is displayed on the display or the touch panel. On the feed pump output setting screen, the feed pump output display area that displays the output of the preset feed pump 24, the feed pump output input area for entering a new feed pump output, the setting button, the return button, the clear button, and the system OFF A button is displayed. Click or tap the back button to return to the initial screen (same for the following back buttons). When the clear button is clicked or tapped, the feed pump output input in the feed pump output input area is deleted, and the feed pump output is re-input in the feed pump output input area (the same applies to the following clear buttons).

  In order to change the output of the feed water pump 24, after inputting the pump output in the feed water pump output input area, the setting button is clicked or tapped. The controller changes the feed pump output displayed in the feed pump output display area to the feed pump output entered in the feed pump output input area, stores the changed feed pump output in the storage area, and displays the system operation screen. Display on the display or touch panel.

  When the circulation pump output setting button is clicked or tapped, a circulation pump output setting screen is displayed on the display or the touch panel. On the circulating pump output setting screen, the circulating pump output display area that displays the output of the circulating pump 49 that has already been set, the circulating pump output input area that inputs a new circulating pump output, the setting button, the return button, the clear button, and the system OFF A button is displayed.

  In order to change the output of the circulation pump 49, after inputting the pump output in the circulation pump output input area, the setting button is clicked or tapped. The controller changes the circulating pump output displayed in the circulating pump output display area to the circulating pump output input in the circulating pump output input area, stores the changed circulating pump output in the storage area, and displays the system operation screen. Display on the display or touch panel.

  Clicking or tapping the rotation speed setting button displays a rotation speed setting screen on the display or touch panel. On the rotation speed setting screen, a rotation speed display area that displays the rotation speed (rotation / h) of the paddle mixer 43a and scraping mixer 43b of the preset stirring and mixing device, a rotation speed input area for inputting a new rotation speed, A setting button, a return button, a clear button, and a system OFF button are displayed.

  To change the rotation speed, enter the rotation speed in the rotation speed input area, and then click or tap the setting button. The controller changes the rotation speed of the paddle mixer 43a and scraping mixer 43b displayed in the rotation speed display area to the rotation speed input in the rotation speed input area, stores the changed rotation speed in the storage area, Displays the system operation screen on the display or touch panel.

  When the oil amount setting button is clicked or tapped, the oil amount setting screen is displayed on the display or the touch panel. On the oil supply amount setting screen, an oil supply amount display area that displays the oil supply amount (liter / h) of the oil supply device 17 that has already been set, an oil supply amount input area for inputting a new oil supply amount, a setting button, a return button, a clear button, The system OFF button is displayed.

  To change the amount of oil to be supplied, enter the amount of oil supplied in the oil supply amount input area, and then click or tap the setting button. The controller changes the lubrication amount of the lubrication device 17 displayed in the lubrication amount display area to the lubrication amount input in the lubrication amount input area, stores the changed lubrication amount in the storage area, and displays the system operation screen. Or on the touch panel.

  After setting or changing the output of the feed water pump 24, the output of the circulation pump 49, the number of revolutions, and the amount of oil supply, clicking or tapping the operation start button on the system operation screen causes the controller to control the control unit of the pure water generator 11 or hydrogen A control unit for the first gas generators 13a to 13c, a control unit for the negative power generators 14a to 14c, a control unit for the second hydrogen gas generator 15, a control unit for the stirring and mixing device 16, a control unit for the oil supply device 17, An activation command is transmitted to the control units of the direction valves 25a to 25j, the control unit of the three-way valve 50, the control unit of the feed pump 24, the control unit of the circulation pump 49, the water level sensor, and the pressure sensor. After receiving the start command from the controller, the pure water generator 11, the hydrogen gas first generators 13a to 13c, the negative power generators 14a to 14c, the hydrogen gas second generator 15, the stirring and mixing device 16, the oil supply device 17, The two-way valves 25a to 25j, the three-way valve 50, the water supply pump 24, the circulation pump 49, each pressure sensor, and the water level sensor are activated.

  When the two-way valves 25a to 25j are activated, the valve mechanisms of the two-way valves 25a to 25j are opened to the set opening, and when the three-way valve 50 is activated, the valve mechanism of the three-way valve 50 is opened to the set opening. When each pressure sensor is activated, the pressure of pure water flowing through the supply pipe 20a is measured by the pressure sensor, and the measured pressure is transmitted to the controller. The pressure of a mixture or compound of high-concentration hydrogen ion water flowing through the circulation pipes 47 and 48 and light oil, kerosene, or heavy oil or a compound is measured by a pressure sensor, and the measured pressure is transmitted to the controller. When the water level sensor is activated, the water level of the mixture (compound) of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil in the stirring tank 42 of the stirring and mixing device 16 is measured by the water level sensor, and the measured water level is transmitted from the water level sensor to the controller. Is done.

  The controller compares the measured pressure transmitted from the pressure sensor with the set pressure, performs feedback control or feedforward control on the feed pump 24 so that the measured pressure falls within the set pressure range, It adjusts so that pure water, hydrogen ion water, and high concentration hydrogen ion water may flow through the water supply pipe 21 and the supply pipes 20a to 20j. The controller compares the measured pressure transmitted from the pressure sensor with the set pressure, performs feedback control or feedforward control on the circulation pump 49 so that the measured pressure falls within the set pressure range, and a predetermined amount of high concentration It adjusts so that the mixture or compound of hydrogen ion water and light oil, kerosene, and heavy oil may flow through the circulation pipes 47 and 48. The controller compares the measured water level transmitted from the water level sensor with the set water level, adjusts the opening degree of the two-way valves 25f, 25g and the three-way valve 50 so that the measured water level falls within the set water level range, and also supplies the fueling device. The amount of light oil, kerosene, and heavy oil supplied from the 17 constant flow device is adjusted.

  When the water supply pump 24 is activated, water is supplied from the water source to the pure water generating device 11 through the water supply pipe 21, and the water supplied from the water source in the pure water generating device 11 is purified (purified water). Process). The pure water that has flowed out of the pure water generator 11 flows into the first hydrotreating device 12a through the supply pipe 20a. In the first hydrotreating apparatus 12a, pure water flows through the drabite porous ceramic 26 accommodated in the flow tank 23, and hydrogen ion water in which hydrogen ions are dissolved is generated from the pure water (hydrogenation process). . The hydrogen ion water that has flowed out of the first hydrotreating device 12a flows into the second hydrotreating device 12b through the supply pipe 20b.

  In the second hydrotreating device 12b, hydrogen ion water flows through the drabite porous ceramic 26 accommodated in the flow tank 23, and more hydrogen ions than the hydrogen ion water generated in the first hydrotreating device 12a. Hydrogen ion water containing is generated (hydrotreating step). The hydrogen ion water flowing out from the second hydrotreating device 12b flows into the third hydrotreating device 12c through the supply pipe 20c. In the third hydrotreating device 12c, hydrogen ion water flows through the drabite porous ceramic 26 accommodated in the flow tank 25, and more hydrogen ions than the hydrogen ion water generated in the second hydrotreating device 12b. Hydrogen ion water containing is generated (hydrotreating step).

  The hydrogen ion water flowing out from the third hydrotreating device 12c flows into the first hydrogen gas first generator 13a through the supply pipe 20d. In the first hydrogen gas first generator 13a, the hydrogen ion water flows between the electrodes 29 (between the cathode and the anode) of the first hydrogen gas first generator 13a, to which the current is passed, so that the hydrogen ion water flows. Electrolyzed to produce high-concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved (electrolysis step). The high-concentration hydrogen ionized water flowing out from the first hydrogen gas first generator 13a flows into the second hydrogen gas first generator 13b through the supply pipe 20e.

  In the second hydrogen gas first generator 13b, high concentration hydrogen ionized water flows between the electrodes 29 (between the cathode and the anode) of the second hydrogen gas first generator 13b to which a current is passed. The hydrogen ion water is electrolyzed, and high concentration hydrogen ion water in which more hydrogen ions are dissolved than the high concentration hydrogen ion water generated by the first hydrogen gas first generator 13a is generated (electrolysis step). The high-concentration hydrogen ion water flowing out from the second hydrogen gas first generator 13b flows into the third hydrogen gas first generator 13c through the supply pipe 20f.

  In the third hydrogen gas first generator 13c, high concentration hydrogen ionized water flows between the electrodes 29 (between the cathode and the anode) of the third hydrogen gas first generator 13c to which a current is passed. The hydrogen ion water is electrolyzed, and high concentration hydrogen ion water in which more hydrogen ions are dissolved than the high concentration hydrogen ion water generated by the second hydrogen gas first generator 13b is generated (electrolysis step). The high-concentration hydrogen ion water that has flowed out of the third hydrogen gas first generator 13c flows into the first negative electrical energizer 30a (first negative power generator 14a) through the supply pipe 20g.

  In the first negative electrical energization device 30a, high-concentration hydrogen ionized water flows between the electrodes 34 (between the cathodes) of the first negative electrical energization device 30a to which a negative current (minus electricity) from the first negative power supply device 31a is energized. By flowing, the minus charge of minus electricity and the plus charge contained in the high concentration hydrogen ion water are combined to generate high concentration hydrogen ion water from which the plus charge is removed (plus charge removing step). The high-concentration hydrogen ionized water that has flowed out of the first negative electrical energization device 30a flows into the second negative electrical energization device 30b (second negative power supply generator 14b) through the supply pipe 20h.

  In the second negative electrical energization device 30b, high-concentration hydrogen ionized water passes between the electrodes 34 (between the cathodes) of the second negative electrical energization device 30b to which a negative current (minus electricity) from the second negative power supply device 31b is energized. By flowing, the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water are combined, and high-concentration hydrogen ion water from which the positive charge is further removed is generated (plus charge removal step). The high-concentration hydrogen ionized water that has flowed out of the second negative electrical energizer 30b flows into the third negative electrical energizer 30c (third negative power generator 14c) through the supply pipe 20i.

  In the third negative electrical energization device 30c, high-concentration hydrogen ionized water passes between the electrodes 34 (between the cathodes) of the third negative electrical energization device 30c to which a negative current (minus electricity) from the third negative power supply device 31c is energized. By flowing, the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water are combined, and high-concentration hydrogen ion water from which the positive charge is further removed is generated (plus charge removal step). The high-concentration hydrogen ion water that has flowed out of the third negative electrical energization device 30c flows into the stirring and mixing device 16 through the supply pipe 20j, and part of it passes through the return pipe 33 to the hydrogen gas second generation device 15. Inflow.

  In the second hydrogen gas generator 15, a part of the high-concentration hydrogen ion water from which the positive charge flowing out from the third negative electric energizer 30c has been removed is the electrode 37 to which the current of the hydrogen gas second generator 15 is energized. The high concentration hydrogen ion water is electrolyzed by flowing between the cathode and the anode, and more hydrogen ions are dissolved than the high concentration hydrogen ion water generated by the third minus electric conduction device 30c. Concentrated hydrogen ion water is generated, and the high concentration hydrogen ion water is made into a mist (mist) by the mist generator 40 and flows into the outgoing pipe 39. The mist-like high-concentration hydrogen ion water flows from the outgoing pipe 39 into the supply pipe 20a and is mixed into pure water flowing through the supply pipe 20a.

  In the compound production system 10A, the hydrogen gas second generator 15 supplies the mist-like high-concentration hydrogen ion water obtained by further electrolyzing a part of the high-concentration hydrogen ion water to the pure water. Since the hydrogenation process in 12c can be promoted, hydrogen ions can be reliably generated in the pure water in the hydrogenation processing apparatuses 12a to 12c, and hydrogen ion water in which a large amount of hydrogen ions are dissolved is reliably produced. In addition, since the electrolysis in the hydrogen gas first generators 13a to 13c can be promoted, a large amount of hydrogen gas can be generated from the hydrogen ion water in the hydrogen gas first generators 13a to 13c. High concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved can be produced reliably.

  The high-concentration hydrogen ion water (high-concentration hydrogen ion water from which the positive charge flowing out from the third negative electric conduction device 30c has been removed) that has flowed into the stirring and mixing device 16 through the supply pipe 20j has an oxidation-reduction potential of −750 mv. Hereinafter, it is preferably −900 mv or less, more preferably −1100 mv or less. A predetermined amount of light oil, kerosene, or heavy oil is supplied to the stirring tank 42 of the storage tank 41 from the oil supply device 17 together with the high-concentration hydrogen ion water. Light oil, kerosene, and heavy oil flow into the agitation tank 42 of the storage tank 41 through the oil supply pipe 52. A mixture of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil is stored from the lower part to the middle part of the stirring tank 42 of the storage tank 41.

  In the agitation tank 42, the high-concentration hydrogen ion water and light oil, kerosene, or heavy oil are agitated and mixed by the paddle mixer 43a and the scraping mixer 43b that are rotated by the rotation of the motor (agitating and mixing step). In the stirring and mixing device 16, the internal pressure of the storage tank 41 is maintained at a high pressure higher than the atmospheric pressure, and the high-concentration hydrogen ion water and light oil, kerosene, or heavy oil are pressurized to a predetermined pressure. Stir and mix. In the agitation / mixing device 16, the high-concentration hydrogen ion water and the light oil, kerosene, or heavy oil are agitated and mixed by the mixers 43 a and 43 b, whereby the high-concentration hydrogen ion water and the light oil, kerosene, or heavy oil are electronically coupled, To change. In the compound manufacturing system 10A, high-concentration hydrogen ionized water, light oil, kerosene, and heavy oil are stirred and mixed under pressure with a predetermined pressure applied in the agitation and mixing device 16 so that high-concentration hydrogen ionized water, light oil, kerosene, and heavy oil Can be quickly and reliably electronically bonded, and a compound containing a large amount of hydrogen ions can be produced.

  A mixture or compound of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil flows into the circulation pipe 48 from the bottom 45 of the storage tank 41 by the circulation pump 49 and passes through the circulation pipe 47 to the stirring tank 42 of the storage tank 41. By being supplied, the circulation pipes 47 and 48 are circulated. In the circulation pipes 47 and 48 extending to the outside of the storage tank 41, a part of the compound flowing through the circulation pipes 47 and 48 by the three-way valve 50 flows into the fuel supply pipe 51, and the compound is supplied to the fuel storage tank 18 or the boiler or generator. And flows into the internal combustion engine 19 such as an engine. When the compound flows into the internal combustion engine 19, the compound burns as fuel in the internal combustion engine 19, and the internal combustion engine 19 operates.

  When light oil is introduced into the stirring tank 42 (stirring mixing device 16) of the storage tank 41, the proportion of the light oil is 60 with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring tank 42 (stirring mixing device 16). It is in the range of -70% by weight. Therefore, in the compound manufacturing system 10A, it is possible to save about 40% to 30% of light oil. If the ratio of light oil to high-concentration hydrogen ion water is less than 60% by weight, the amount of heat of the compound made from the high-concentration hydrogen ion water and light oil decreases, the combustion energy decreases, and the internal combustion engine 19 can be driven sufficiently. Can not. When the ratio of the light oil to the high concentration hydrogen ion water exceeds 70% by weight, the high concentration hydrogen ion water and the light oil cannot be electronically bonded quickly.

  When kerosene is charged into the stirring tank 42 (stirring mixing device 16) of the storage tank 41, the ratio of the kerosene is 50% with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring tank 42 (stirring mixing device 16). It is in the range of -70% by weight. Therefore, in the compound manufacturing system 10A, about 50% to 30% of kerosene can be saved. If the ratio of kerosene to high-concentration hydrogen ion water is less than 50% by weight, the amount of heat of the compound made from the high-concentration hydrogen ion water and kerosene decreases, the combustion energy decreases, and the internal combustion engine 19 can be driven sufficiently. Can not. If the ratio of kerosene to high-concentration hydrogen ion water exceeds 70% by weight, the high-concentration hydrogen ion water and kerosene cannot be electronically coupled quickly.

  When heavy oil is charged into the stirring tank 42 (stirring and mixing device 16) of the storage tank 41, the ratio of the heavy oil is 50 with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring tank 42 (stirring and mixing device 16). It is in the range of -70% by weight. Therefore, the compound production system 10A can save about 50% to 30% of heavy oil. If the ratio of heavy oil to high-concentration hydrogen ion water is less than 50% by weight, the amount of heat of the compound made from the high-concentration hydrogen ion water and heavy oil decreases, the combustion energy decreases, and the internal combustion engine 19 can be driven sufficiently. Can not. If the ratio of heavy oil to high concentration hydrogen ion water exceeds 70% by weight, the high concentration hydrogen ion water and heavy oil cannot be electronically bonded quickly.

  The compound manufacturing system 10A purifies the water supplied from the water source by the pure water generation device 11, generates hydrogen ion water in which hydrogen ions are dissolved by the hydrogenation processing devices 12a to 12c, and the hydrogen gas first generation device 13a. High concentration hydrogen ion water from which high concentration hydrogen ion water is generated from hydrogen ion water by ˜13c, and positive charges are removed by negative power source generators 14a-14c (negative electric current supply devices 30a-30c, negative power source devices 31a-31c) Ionized water is generated, and a high-concentration hydrogen ionized water and light oil, kerosene, or heavy oil are electronically combined with the stirring and mixing device 16 to form a compound, and a large amount of hydrogen ions are dissolved in the compound. ) And hydrogen burns together, greatly improving combustion efficiency compared to burning only fuel. It is possible to make bets capable compound.

In the compound production system 10A, since the compound produced thereby is an electronic combination of light oil, kerosene, heavy oil (fossil fuel) and high-concentration hydrogen ion water, light oil, kerosene, heavy oil containing light oil, Compared with the case where only kerosene and heavy oil are used, the amount of light oil, kerosene and heavy oil can be reduced, and depletion of fossil fuels can be delayed. In the compound manufacturing system 10A, hydrogen that does not generate soot is burned together with light oil, kerosene, and heavy oil (fossil fuel). Therefore, compared with the case where only light oil, kerosene, and heavy oil are burned, the compound in which the generation of smoke is significantly suppressed. It is possible to make a compound that can prevent air pollution during combustion. Since the compound manufacturing system 10A can produce a compound that suppresses the generation of soot, it does not require equipment such as a filter or a catalyst that removes soot during combustion in the internal combustion engine 19 such as a boiler, a generator, or an engine. Since water costs are not incurred by using water existing in the natural world, a compound can be produced at a low price and a compound having a low unit price can be produced.
FIG. 8 is a configuration diagram of a compound manufacturing system 10 </ b> B shown as another example, and FIG. 9 is a diagram showing an example of the magnetic processing device 53. FIG. 10 is a diagram illustrating an example of the ion exchange filter device 57. The compound production system 10B includes a pure water generation device 11, a hydrogenation processing device 12 (mineral decomposition device), a hydrogen gas first generation device 13 (first electrolysis device), a negative power supply generation device 14, a magnetic processing device 53, or an ion. The exchange filter device 57, the hydrogen gas second generator 15 (second electrolysis device), the stirring and mixing device 16, and the oil supply device 17 are formed. A fuel storage tank 18 or an internal combustion engine 19 such as a boiler, a generator, or an engine is connected to the compound manufacturing system 10B.

  The compound manufacturing system 10B uses a compound to be used as a fuel for the internal combustion engine 19 through a pure water purification process, a hydrogenation process, an electrolysis process, a positive charge removal process (a negative electric current application process), an oxygen ion removal process, and a stirring and mixing process. To manufacture. In the compound production system 10B, these devices 11, 12, 13, 14, 15, 53, 57 are the pure water generator 11 → the hydrogenation processor 12 → the hydrogen gas first generator 13 → the negative power source generator 14 → the magnetic treatment. The devices 53 or the ion exchange filter device 57 are arranged in the order of the stirring and mixing device 15. In the compound manufacturing system 10B, either the magnetic processing device 53 or the ion exchange filter device is used, but both the magnetic processing device 53 and the ion exchange filter device may be used. In this case, the magnetic processing device 53 is arranged in the order of the ion exchange filter device 57, or the ion exchange filter device 57 is arranged in the order of the magnetic processing device 53.

  The pure water generator 11 is the same as that of the compound production system 10A of FIG. 1, purifies water supplied from a water source, and supplies the pure water to the hydrotreating device 12. The pure water generator 11 is connected (connected) to a water source by a water supply pipe 21 through which water flows, and is connected (connected) to the hydrotreating apparatus 12 by a supply pipe 20a through which pure water flows. The water source and water are the same as those of the compound manufacturing system 10A of FIG.

  The hydrotreating apparatus 12 is the same as that of the compound manufacturing system 10A of FIG. 1, performs a hydrotreating process that generates hydrogen ions in pure water, and generates hydrogen ion water in which hydrogen ions are dissolved. The hydrotreating device 12 is formed of a storage container 22 that is long in one direction having an inflow port and an outflow port, and a flow tank 23 having a predetermined volume formed inside the storage container 22 (referring to FIG. 2). . In the compound manufacturing system 10 </ b> B, three first to third hydroprocessing apparatuses 12 a to 12 c are installed. These hydrogenation processing apparatuses 12a to 12c are arranged in the order of the first hydrogenation processing apparatus 12a → the second hydrogenation processing apparatus 12b → the third hydrogenation processing apparatus 12c.

  A water supply pump 24 is installed in the supply pipe 20a extending between the pure water generator 11 and the first hydrotreating apparatus 12a, and the supply pipe 20a is connected to the supply pipe 20a extending immediately downstream of the water supply pump 24. A pressure sensor (not shown) for measuring the pressure of pure water flowing therethrough is installed. A two-way valve 25a (solenoid valve) is installed in the supply pipe 20a extending in the immediate vicinity of the first hydrotreating device 12a. A plurality of drabite porous ceramics 26 (mineral containing magnesium as a main component) are accommodated in the flow tanks 23 of the hydrotreating apparatuses 12a to 12c.

  The first hydrogen gas generator 13 is the same as that of the compound production system 10A of FIG. 1, and generates hydrogen gas by electrolyzing hydrogen ion water, and high-concentration hydrogen in which a large amount of hydrogen ions are dissolved from the hydrogen ion water. Ionized water is produced. The first hydrogen gas generator 13 includes a storage container 27 that is long in one direction having an inlet and an outlet, an electrode tank 28 having a predetermined volume formed inside the storage container 27, and a plurality of containers stored in the electrode tank 28. It is formed from a sheet of electrodes 29 (cathode and anode) (with reference to FIG. 3). In the compound manufacturing system 10B, three first to third hydrogen gas first generators 13a to 13c are installed. The first hydrogen gas generators 13 are arranged in the order of the first hydrogen gas first generator 13a → the second hydrogen gas first generator 13b → the third hydrogen gas first generator 13c.

  A two-way valve 25b (solenoid valve) is installed in the supply pipe 20d extending between the third hydrotreating device 12c and the first hydrogen gas first generator 13a. The electrodes 29 (cathode and anode) include a mesh electrode 29 having a predetermined area made of a titanium alloy, a mesh electrode 29 having a predetermined area made of an iridium oxide alloy, and a predetermined electrode made of a carbon nanotube. Any one of mesh-shaped electrodes 29 having an area is used.

  The negative power source generator 14 is the same as that of the compound manufacturing system 10A of FIG. 1, and combines a negative charge of negative electricity and a positive charge contained in the high concentration hydrogen ion water to generate a positive charge from the high concentration hydrogen ion water. The high concentration hydrogen ion water from which the positive charge is removed is generated. The negative power supply generator 14 is formed of negative electrical energization devices 30a to 30c and negative power supply devices 31a to 31c. In the compound manufacturing system 10B, three first to third negative power generators 14a to 14c are installed. These negative power generators 14 are arranged in the order of the first negative power generator 14a → the second negative power generator 14b → the third negative power generator 14c.

  The negative electrical current supply devices 30a to 30c and the negative power supply devices 31a to 31c are the same as those of the compound production system 10A of FIG. The negative electrical energization devices 30 a to 30 c are each composed of a storage container 32 that is long in one direction having an inlet and an outlet, an electrode tank 33 having a predetermined volume formed inside the storage container 32, and a plurality of containers stored in the electrode tank 33. It forms from the electrode 34 (cathode and anode) of a sheet | seat (FIG. 4 assistance). A two-way valve 25b (solenoid valve) is installed in the supply pipe 20d extending between the third hydrogen gas first generator 13c and the first negative power source generator 14a (first negative electrical energizer 30a). . The electrode 34 (cathode and anode) includes a mesh electrode 34 having a predetermined area made of a titanium alloy, a mesh electrode 34 having a predetermined area made of an iridium oxide alloy, and a constant electrode made of carbon nanotubes. Any one of mesh-shaped electrodes 34 having an area is used.

  The magnetic processing device 53 performs a magnetic treatment for removing oxygen ions dissolved in the high-concentration hydrogen ion water from which the positive charge generated by the negative power source generator 14 is removed, and the high concentration from which oxygen ions (oxygen) are removed. Produces hydrogen ion water. The magnetic processing device 53 includes a container 54 that is long in one direction having an inlet and an outlet, a magnetic tank 55 having a predetermined volume formed inside the container 54, and a permanent magnet 56 that is stored in the magnetic tank 55. Formed from. When the magnetic processing apparatus 53 is used in the compound manufacturing system 10B, three first to third magnetic processing apparatuses 53a to 53c are installed in the compound manufacturing system 10B. Note that one or two magnetic processing devices 53 may be installed or four or more magnetic processing devices 53 may be installed depending on the amount of high-concentration hydrogen ion water produced from which oxygen ions are removed. The first to third magnetic processing devices 53a to 53c are arranged in the order of the first magnetic processing device 53a → the second magnetic processing device 53b → the third magnetic processing device 53c.

  The first magnetic processing device 53a is disposed on the downstream side of the third negative power supply generator 14c (third negative electrical energization device 30c), and is connected (connected) to the third negative power supply generator 14c by the supply pipe 20k. . The supply pipe 20k is connected to the outlet of the third negative power generator 14c and the inlet of the first magnetic processing device 53a. A two-way valve 25h (solenoid valve) is installed in the supply pipe 20k. The second magnetic processing device 53b is disposed on the downstream side of the first magnetic processing device 53a, and is connected (connected) to the first magnetic processing device 53a by a supply pipe 201. The supply pipe 201 is connected to the outlet of the first magnetic processing device 53a and the inlet of the second magnetic processing device 53b. The third magnetic processing device 53c is disposed on the downstream side of the second magnetic processing device 53b, and is connected (connected) to the second magnetic processing device 53b by the supply pipe 20m. The supply pipe 20m is connected to the outlet of the second magnetic processing device 53b and the inlet of the third magnetic processing device 53c.

  The permanent magnet 56 is accommodated in the magnetic tank 55 of the magnetic processing devices 53a to 53c. The permanent magnet 56 has a surface magnetic force in the range of 2000 to 7000 gauss, preferably in the range of 4000 to 7000 gauss. In these magnetic processing devices 53 a to 53 c, oxygen ions dissolved in the high-concentration hydrogen ion water by the magnetic force of the permanent magnet 56 are passed by passing the high-concentration hydrogen ion water between the permanent magnets 56 accommodated in the magnetic tank 55. It is removed (oxygen ions flow from the permanent magnet 56 to the ground (not shown)), and high-concentration hydrogen ion water from which oxygen ions are removed is generated. In the compound manufacturing system 10B, by using the three magnetic processing devices 53a to 53c, oxygen ions can be reliably removed from the high-concentration hydrogen ion water, and the high-concentration hydrogen ion water from which the oxygen ions have been removed is removed. Can be generated.

  The ion exchange filter device 57 removes oxygen ions dissolved in the high-concentration hydrogen ion water from which the positive charges generated by the negative power source generator 14 are removed, and the high-concentration hydrogen ion water from which oxygen ions (oxygen) are removed. Is generated. The ion exchange filter device 57 includes a storage container 58 that is long in one direction having an inlet and an outlet, a filter tank 59 having a predetermined volume formed inside the storage container 58, and an ion exchange filter that is stored in the filter tank 59. 60. When the ion exchange filter device 57 is used in the compound production system 10B, three first to third ion exchange filter devices 57a to 57c are installed in the compound production system 10B. One or two ion exchange filter devices 57 may be installed or four or more ion exchange filter devices 57 may be installed according to the amount of high-concentration hydrogen ion water produced from which oxygen ions have been removed. Good. The first to third ion exchange filter devices 57a to 57c are arranged in the order of the first ion exchange filter device 57a → the second ion exchange filter device 57b → the third ion exchange filter device 57c.

  The first ion exchange filter device 57a is disposed on the downstream side of the third negative power generator 14c (third negative electric current supply device 30c), and is connected (connected) to the third negative power generator 14c by the supply pipe 20k. Yes. The supply pipe 20k is connected to the outlet of the third negative power generator 14c and the inlet of the first ion exchange filter device 57a. The second ion exchange filter device 57b is arranged on the downstream side of the first ion exchange filter device 57a, and is connected (connected) to the first ion exchange filter device 57a by the supply pipe 201. The supply pipe 201 is connected to the outlet of the first ion exchange filter device 57a and the inlet of the second ion exchange filter device 57b. The third ion exchange filter device 57c is disposed on the downstream side of the second ion exchange filter device 57b, and is connected (connected) to the second ion exchange filter device 57b by the supply pipe 20m. The supply pipe 20m is connected to the outlet of the second ion exchange filter device 57b and the inlet of the third ion exchange filter device 57c.

  The ion exchange filter 60 is accommodated in the filter tank 59 of the ion exchange filter devices 57a to 57c. In these ion exchange filter devices 57a to 57c, high-concentration hydrogen ion water passes through (passes) the ion exchange filter 60 accommodated in the filter tank 59, so that oxygen dissolved in the high-concentration hydrogen ion water by the ion exchange filter 60. Ions are removed, and high-concentration hydrogen ion water from which oxygen ions are removed is generated. In the compound manufacturing system 10B, by using the three ion exchange filter devices 57a to 57c, oxygen ions can be reliably removed from the high concentration hydrogen ion water, and the high concentration hydrogen ion water from which the oxygen ions have been removed. Can be generated.

  The hydrogen gas second generation device 15 is the same as that of the compound production system 10A of FIG. 1, and high-concentration hydrogen ions from which oxygen ions generated by the magnetic processing devices 53a to 53c or the ion exchange filter devices 57a to 57c are removed. A portion of the water is extracted, and a portion of the high-concentration hydrogen ion water is electrolyzed to generate hydrogen gas and a mist-like high-concentration hydrogen ion water is generated. Supply to pure water (supply pipe 20a). The second hydrogen gas generator 15 includes a container 35 that is long in one direction having an inlet and an outlet, an electrode tank 36 having a predetermined volume formed inside the container 35, and a plurality of containers stored in the electrode tank 36. It is formed from a sheet of electrodes 37 (cathode and anode) (with reference to FIG. 5). The hydrogen gas second generator 15 accommodates a mist generator 40 that makes high-concentration hydrogen ionized water mist (mist) by ultrasonic vibration.

  The second hydrogen gas generator 15 is disposed on the downstream side of the third magnetic processing device 53c or the third ion exchange filter device 57c, and is connected to the third magnetic processing device 53c or the third ion exchange filter device 57c by the return pipe 38. (Connected) and connected (connected) to the supply pipe 20 a by the forward pipe 39. The return pipe 38 is connected to the vicinity of the outlet of the third magnetic processing device 53 c or the third ion exchange filter device 57 c and the inlet of the hydrogen gas second generator 15. The outgoing pipe 39 is connected to the outlet of the second hydrogen gas generator 15 and the supply pipe 20 a extending upstream of the feed water pump 24. A two-way valve 25 g is installed in the outgoing pipe 39 extending in the vicinity of the hydrogen gas second generator 15. The electrode 37 includes a mesh electrode 37 having a predetermined area made of a titanium alloy, a mesh electrode 37 having a predetermined area made of an iridium oxide alloy, and a mesh having a predetermined area made of carbon nanotubes. One of the electrodes 37 is used.

  The stirring and mixing device 16 is the same as that of the compound manufacturing system 10A of FIG. 1, and a predetermined fuel is added to the high concentration hydrogen ion water generated by the magnetic processing devices 53a to 53c or the ion exchange filter devices 57a to 57c. Concentrated hydrogen ion water and fuel are stirred and mixed, and high concentration hydrogen ion water and fuel are electronically coupled to form a compound. The stirring and mixing device 16 includes a storage tank 41 that is long in one direction, a stirring tank 42 having a predetermined volume formed inside the storage tank 41, a paddle mixer 43a and a scraping mixer 43b that are installed below the stirring tank 42, , A water level sensor (not shown) for measuring the water level of a mixture (compound) of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil in the stirring tank 42, and a motor (not shown) for rotating the mixers 43a and 43b (Refer to FIG. 5). The inside of the storage tank 41 is maintained at a pressure higher than the atmospheric pressure.

  The stirring and mixing device 16 is disposed downstream of the third magnetic processing device 53c or the third ion exchange filter device 57c, and is connected (connected) to the third magnetic processing device 53c or the third ion exchange filter device 57c by the supply pipe 20j. Has been. The supply pipe 20j is connected to the outlet of the third magnetic processing device 53c or the third ion exchange filter device 57c and the side portion 44 of the storage tank 41 of the stirring and mixing device 16. A two-way valve 25e (electromagnetic valve) is installed in the supply pipe 20j. Circulation pipes 47 and 48 are connected to the top 46 and the low part 45 of the storage tank 41. A two-way valve 25 f (electromagnetic valve) and a circulation pump 49 are installed in a circulation pipe 48 extending from the lower portion 45 of the storage tank 41 to the outside of the storage tank 41. A pressure sensor (not shown) for measuring the pressure of a mixture (compound) of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil flowing through the circulation pipe 48 is provided in the circulation pipe 48 extending downstream of the circulation pump 49. And a three-way valve 50 (solenoid valve). An oil supply pipe 51 connected to the fuel storage tank 18 or the internal combustion engine 19 is connected to the three-way valve 50.

  The oil supply device 17 is the same as that of the compound production system 10 </ b> A of FIG. 1, and stores any of light oil, kerosene, and heavy oil (fossil fuel), and supplies light oil, kerosene, and heavy oil to the stirring and mixing device 16. The oil supply device 17 includes a constant flow device (not shown), and a constant amount of light oil, kerosene, or heavy oil (liter / h) is supplied to the stirring and mixing device 16 by the constant flow device. The oil supply device 17 is connected to the stirring and mixing device 16 by an oil supply pipe 52. The oil supply pipe 52 is provided with a two-way valve 25g (electromagnetic valve).

  Control unit of pure water generation device 11, control unit of hydrogen gas first generation devices 13 a to 13 c, control unit of negative power source generation devices 14 a to 14 c, control unit of hydrogen gas second generation device 15, stirring and mixing device 16 The control unit of the oil supply device 17, the water level sensor, each pressure sensor, the control unit of these two-way valves 25a to 25h, the control unit of the three-way valve 50, the control unit of the feed water pump 24, the control unit of the circulation pump 50 are Are connected to a controller (not shown) via a control signal line (wired or wireless). The controller is the same as that of the compound manufacturing system 10A of FIG.

  FIG. 11 is a configuration diagram of the compound manufacturing system 10B shown in an operating state. In FIG. 11, the flow of water, pure water, hydrogen ion water, high-concentration hydrogen ion water, or a compound is indicated by arrows. In order to operate the compound manufacturing system 10B, the controller is turned on to activate the controller, and an initial screen is displayed on the display or touch panel. Click or tap the system ON button on the initial screen to display the system operation screen on the display or touch panel. On the system operation screen, an operation start button, a system OFF button, a feed water pump output setting button, a circulation pump output setting button, a rotation speed setting button, and an oil supply amount setting button are displayed. The procedure for changing the output of the feed water pump 24, the procedure for changing the output of the circulation pump 50, the procedure for changing the number of revolutions, and the procedure for changing the amount of oil supply are the same as those of the compound production system 10A of FIG.

  After setting or changing the output of the feed water pump 24, the output of the circulation pump 50, the number of revolutions, and the amount of oil supply, clicking or tapping the operation start button on the system operation screen, the pure water generator 11 or the hydrogen gas first generator 13a To 13c, negative power source generators 14a to 14c, hydrogen gas second generator 15, agitation and mixing device 16, oil supply device 17, two-way valve 25a to 25g, three-way valve 50, water supply pump 24, circulation pump 49, each pressure sensor The water level sensor is activated. When the two-way valves 25a to 25g are activated, the valve mechanisms of the two-way valves 25a to 25g are opened to the set opening, and when the three-way valve 50 is activated, the valve mechanism of the three-way valve 50 is opened to the set opening. When each pressure sensor is activated, the pressure of pure water flowing through the supply pipe 20a is measured by the pressure sensor, and the measured pressure is transmitted to the controller. The pressure of a mixture or compound of high-concentration hydrogen ion water flowing through the circulation pipes 47 and 48 and light oil, kerosene, or heavy oil or a compound is measured by a pressure sensor, and the measured pressure is transmitted to the controller. When the water level sensor is activated, the water level of the mixture (compound) of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil in the stirring tank 42 of the stirring and mixing device 16 is measured by the water level sensor, and the measured water level is transmitted from the water level sensor to the controller. Is done.

  The controller adjusts so that a predetermined amount of water, pure water, hydrogen ion water, high-concentration hydrogen ion water flows through the water supply pipe 21 and the supply pipes 20a to 20m, similarly to the compound production system 10A of FIG. A mixture or compound of a predetermined amount of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil is adjusted to flow through the circulation pipes 47 and 48, and the opening degree of the two-way valves 25f and 25g and the three-way valve 50 is adjusted. Then, the amount of light oil, kerosene, or heavy oil supplied from the constant flow device of the oil supply device 17 is adjusted.

  Water is supplied from the water source to the pure water generator 11 through the water supply pipe 21, and the pure water generator 11 purifies the water (pure water purification process). The pure water that has flowed out of the pure water generator 11 flows into the first hydrotreating device 12a through the supply pipe 20a. In the first hydrotreating apparatus 12a, pure water flows through the drabite porous ceramic 26 accommodated in the flow tank 23, and hydrogen ion water in which hydrogen ions are dissolved is generated from the pure water (hydrogenation process). . The hydrogen ion water that has flowed out of the first hydrotreating device 12a flows into the second hydrotreating device 12b through the supply pipe 20b.

  In the second hydrotreating device 12b, hydrogen ion water flows through the drabite porous ceramic 26 accommodated in the flow tank 23, and more hydrogen ions than the hydrogen ion water generated in the first hydrotreating device 12a. Hydrogen ion water containing is generated (hydrotreating step). The hydrogen ion water flowing out from the second hydrotreating device 12b flows into the third hydrotreating device 12c through the supply pipe 20c. In the third hydrotreating device 12c, hydrogen ion water flows through the drabite porous ceramic 26 accommodated in the flow tank 23, and more hydrogen ions than the hydrogen ion water generated in the second hydrotreating device 12b. Hydrogen ion water containing is generated (hydrotreating step).

  The hydrogen ion water flowing out from the third hydrotreating device 12c flows into the first hydrogen gas first generator 13a through the supply pipe 20d. In the first hydrogen gas first generator 13a, the hydrogen ion water is electrolyzed by passing the hydrogen ion water between the electrodes 29 (between the cathode and the anode), and high concentration hydrogen ions in which a large amount of hydrogen ions are dissolved. Water is produced (electrolysis process). The high-concentration hydrogen ionized water flowing out from the first hydrogen gas first generator 13a flows into the second hydrogen gas first generator 13b through the supply pipe 20e.

In the second hydrogen gas first generator 13b, the high-concentration hydrogen ion water is electrolyzed by passing the high-concentration hydrogen ion water between the electrodes 29 (between the cathode and the anode), and the first hydrogen gas first generation is performed. High concentration hydrogen ion water in which more hydrogen ions are dissolved than the high concentration hydrogen ion water generated by the apparatus 13a is generated (electrolysis step). The high-concentration hydrogen ion water flowing out from the second hydrogen gas first generator 13b flows into the third hydrogen gas first generator 13c through the supply pipe 20f. In the third hydrogen gas first generator 13c, the high concentration hydrogen ion water is electrolyzed by flowing between the electrodes 29 (between the cathode and the anode), and the second hydrogen gas first generation is performed. High concentration hydrogen ion water in which more hydrogen ions are dissolved than the high concentration hydrogen ion water generated by the apparatus 13b is generated (electrolysis step).

  The high-concentration hydrogen ion water that has flowed out of the third hydrogen gas first generator 13c flows into the first negative electrical energizer 30a (first negative power generator 14a) through the supply pipe 20g. In the first negative electrical energization device 30a, the high-concentration hydrogen ion water flows between the electrodes 34 (between the cathodes), so that the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water are combined. Then, high-concentration hydrogen ion water from which positive charges have been removed is generated (plus charge removal step). The high-concentration hydrogen ionized water that has flowed out of the first negative electrical energization device 30a flows into the second negative electrical energization device 30b (second negative power supply generator 14b) through the supply pipe 20h.

  In the second negative electrical energization device 30b, the high-concentration hydrogen ion water flows between the electrodes 34 (between the cathodes), so that the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water are combined. Further, high-concentration hydrogen ion water from which the positive charges have been removed is generated (plus charge removal step). The high-concentration hydrogen ionized water that has flowed out of the second negative electrical energizer 30b flows into the third negative electrical energizer 30c (third negative power generator 14c) through the supply pipe 20i. In the third negative electrical energization device 30c, the high-concentration hydrogen ion water flows between the electrodes 34 (between the cathodes), so that the negative charge of negative electricity and the positive charge contained in the high-concentration hydrogen ion water are combined. Further, high-concentration hydrogen ion water from which the positive charges have been removed is generated (plus charge removal step).

  The high-concentration hydrogen ionized water that has flowed out of the third negative electrical energization device 30c flows into the first magnetic processing device 53a or the first ion exchange filter device 57a through the supply pipe 20k. In the first magnetic processing device 53a or the first ion exchange filter device 57a, the high-concentration hydrogen ion water passes through the permanent magnet 56 accommodated in the magnetic tank 55 or the ion exchange filter 60 accommodated in the filter tank 59. Oxygen ions dissolved in the high-concentration hydrogen ion water are removed, and high-concentration hydrogen ion water from which oxygen ions have been removed is generated (oxygen ion removal step). The high-concentration hydrogen ion water flowing out from the first magnetic processing device 53a or the first ion exchange filter device 57a flows into the second magnetic processing device 53b or the second ion exchange filter device 57b through the supply pipe 201.

  In the second magnetic processing device 53b or the second ion exchange filter device 57b, the high-concentration hydrogen ion water passes through the permanent magnet 56 housed in the magnetic tank 55 or the ion exchange filter 60 housed in the filter tank 59. High-concentration hydrogen ion water from which oxygen ions dissolved in the high-concentration hydrogen ion water are removed and oxygen ions are removed from the high-concentration hydrogen ion water generated by the first magnetic processing device 53a or the first ion exchange filter device 57a. Is generated (oxygen ion removing step). The high-concentration hydrogen ion water flowing out from the second magnetic processing device 53b or the second ion exchange filter device 57b flows into the third magnetic processing device 53c or the third ion exchange filter device 57c through the supply pipe 20m.

  In the third magnetic processing device 53c or the third ion exchange filter device 57c, the high-concentration hydrogen ion water passes through the permanent magnet 56 accommodated in the magnetic tank 55 or the ion exchange filter 60 accommodated in the filter tank 59. High-concentration hydrogen ion water from which oxygen ions dissolved in the high-concentration hydrogen ion water are removed and oxygen ions are removed from the high-concentration hydrogen ion water generated by the second magnetic processing device 53b or the second ion exchange filter device 57b. Is generated (oxygen ion removing step). The high-concentration hydrogen ionized water that has flowed out of the third magnetic processing device 53c or the third ion exchange filter device 57c flows into the mixing and stirring device 16 through the supply pipe 20j, and part of it passes through the return pipe 33 to form hydrogen. It flows into the gas second generator 15. The compound manufacturing system 10B can make high-concentration hydrogen ion water from which oxygen ions (dissolved oxygen) have been removed by the magnetic processing devices 53a to 53c or the ion exchange filter devices 57a to 57c. High-concentration hydrogen ion water in which hydrogen ions are dissolved can be produced.

  In the hydrogen gas second generator 15, a part of the high-concentration hydrogen ion water flowing from the third magnetic processing device 53 c or the third ion exchange filter device 57 c flows between the electrodes 37 (between the cathode and the anode). The high-concentration hydrogen ion water is electrolyzed to generate high-concentration hydrogen ion water in which more hydrogen ions are dissolved than the high-concentration hydrogen ion water generated by the third hydrogen gas first generator 13c. High-concentration hydrogen ionized water is mist-like (mist-like) by the mist generator 40 and flows into the outgoing pipe 39. The mist-like high-concentration hydrogen ion water flows from the outgoing pipe 39 into the supply pipe 20a and is mixed into pure water flowing through the supply pipe 20a.

  In the compound production system 10B, the hydrogen gas second generator 15 supplies the mist-like high-concentration hydrogen ion water obtained by further electrolyzing a part of the high-concentration hydrogen ion water to the pure water, so Since the hydrogenation process in 12c can be promoted, hydrogen ions can be reliably generated in the pure water in the hydrogenation processing apparatuses 12a to 12c, and hydrogen ion water in which a large amount of hydrogen ions are dissolved is reliably produced. In addition, since the electrolysis in the hydrogen gas first generators 13a to 13c can be promoted, a large amount of hydrogen gas can be generated from the hydrogen ion water in the hydrogen gas first generators 13a to 13c. High concentration hydrogen ion water in which a large amount of hydrogen ions are dissolved can be produced reliably.

  High-concentration hydrogen ion water (high-concentration hydrogen ion water flowing out from the third magnetic processing device 53c or the third ion exchange filter device 57c) flowing into the stirring and mixing device 16 through the supply pipe 20j has a redox potential of − It is 750 mv or less, preferably -900 mv or less, more preferably -1100 mv or less. A predetermined amount of light oil, kerosene, or heavy oil is supplied to the stirring tank 42 of the storage tank 41 from the oil supply device 17 together with the high-concentration hydrogen ion water. Light oil, kerosene, and heavy oil flow into the agitation tank 42 of the storage tank 41 through the oil supply pipe 52. A mixture of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil is stored from the lower part to the middle part of the stirring tank 42 of the storage tank 41.

  In the agitation tank 42, the high-concentration hydrogen ion water and light oil, kerosene, or heavy oil are agitated and mixed by the paddle mixer 43a and the scraping mixer 43b that are rotated by the rotation of the motor (agitating and mixing step). In the stirring and mixing device 16, the internal pressure of the storage tank 415 is maintained at a high pressure higher than the atmospheric pressure, and the high-concentration hydrogen ion water and light oil, kerosene, or heavy oil are pressurized to a predetermined pressure. Stir and mix. In the agitation / mixing device 16, the high-concentration hydrogen ion water and the light oil, kerosene, or heavy oil are agitated and mixed by the mixers 43 a and 43 b, whereby the high-concentration hydrogen ion water and the light oil, kerosene, or heavy oil are electronically coupled, To change.

  In the compound production system 10B, high-concentration hydrogen ionized water, light oil, kerosene, and heavy oil are agitated and mixed under a pressure applied with a predetermined pressure in the agitation and mixing device 16 so that high-concentration hydrogen ionized water, light oil, kerosene, and heavy oil Can be quickly and reliably electronically bonded, and a compound containing a large amount of hydrogen ions can be produced. A mixture or compound of high-concentration hydrogen ion water and light oil, kerosene, or heavy oil flows into the circulation pipe 48 from the bottom 45 of the storage tank 41 by the circulation pump 49 and passes through the circulation pipe 47 to the stirring tank 42 of the storage tank 41. By being supplied, the circulation pipes 47 and 48 are circulated. In the circulation pipe 48 extending to the outside of the storage tank 41, a part of the compound flowing through the circulation pipe 48 by the three-way valve 50 flows into the fuel supply pipe 51, and the compound is injected into the fuel storage tank 18 or the boiler, generator, engine, etc. It flows into the internal combustion engine 19.

  The ratio of the light oil charged into the stirring tank 42 (stirring mixing device 16) of the storage tank 41 is the same as that of the compound production system 10A of FIG. 1, and is 60 to 70 wt% with respect to 100 wt% of high-concentration hydrogen ionized water. % Range. The ratio of kerosene charged into the stirring tank 42 of the storage tank 41 is the same as that of the compound production system 10A of FIG. 1, and is in the range of 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water. The ratio of heavy oil charged into the stirring tank 42 of the storage tank 41 is the same as that of the compound production system 10A of FIG. 1, and is in the range of 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water.

  The compound manufacturing system 10B purifies the water supplied from the water source by the pure water generation device 11, generates hydrogen ion water in which hydrogen ions are dissolved by the hydrogenation processing devices 12a to 12c, and the hydrogen gas first generation device 13a. High concentration hydrogen ion water from which high concentration hydrogen ion water is generated from hydrogen ion water by ˜13c, and positive charges are removed by negative power source generators 14a-14c (negative electric current supply devices 30a-30c, negative power source devices 31a-31c) Ionized water is generated, high concentration hydrogen ionized water from which oxygen ions are removed by the magnetic processing devices 53a to 53c or ion exchange filter devices 57a to 57c is generated, and the high concentration hydrogen ionized water and light oil or kerosene are generated by the stirring and mixing device 16. , A heavy oil is electronically bonded to make a compound, and the compound contains many hydrogen ions. Dissolved in, because the hydrogen together with the fuel during combustion is burnt, compared with the case of burning only the fuel can be made a compound capable to significantly improve the combustion efficiency.

  In the compound production system 10B, the compound produced thereby is an electronic combination of light oil, kerosene, heavy oil (fossil fuel) and high-concentration hydrogen ionized water. Compared with the case where only kerosene and heavy oil are used, the amount of light oil, kerosene and heavy oil can be reduced, and depletion of fossil fuels can be delayed. Since the compound production system 10B burns hydrogen that does not generate soot together with light oil, kerosene, and heavy oil, it can produce a compound in which the generation of soot is significantly suppressed compared to the case of burning only light oil, kerosene, and heavy oil. It is possible to make a compound that can prevent air pollution during combustion. Since the compound manufacturing system 10B can produce a compound that suppresses the generation of soot, it does not require equipment such as a filter or a catalyst that removes soot during combustion in the internal combustion engine 18 such as a boiler, a generator, or an engine. Since water costs are not incurred by using water existing in the natural world, a compound can be produced at a low price and a compound having a low unit price can be produced.

DESCRIPTION OF SYMBOLS 10A Compound manufacturing system 10B Compound manufacturing system 11 Pure water production | generation apparatus 12 Hydrotreating apparatus 12a 1st hydrotreating apparatus 12b 2nd hydrotreating apparatus 12c 3rd hydrotreating apparatus 13 Hydrogen gas 1st generator 13a 1st hydrogen Gas first generator 13b Second hydrogen gas first generator 13c Third hydrogen gas first generator 14 Negative power source generator 14a First negative power source generator 14b Second negative power source generator 14c Third negative power source generator 15 Hydrogen gas second generating device 16 Stirring and mixing device 17 Refueling device 18 Fuel storage tank 19 Internal combustion engine 20a to 20j Supply pipe 21 Water supply pipe 22 Storage container 23 Flow tank 24 Water supply pump 25a to 25f Two-way valve 26 Drabite porous ceramic 27 Container 28 Electrode tank 29 Electrode 30a First minor 30c Second negative electric current supply device 30c Third negative electric current supply device 31a First negative power supply device 31b Second negative power supply device 31c Third negative power supply device 32 Storage container 33 Electrode tank 34 Electrode 35 Storage container 36 Electrode tank 37 Electrode 38 Return pipe 39 Outgoing pipe 40 Mist generator 41 Storage tank 42 Stirring tank 43a Paddle mixer 43b Scraping mixer 44 Side 45 Bottom 46 Top 47 Circulation pipe 48 Circulation pipe 48 Circulation pump 50 Three-way valve 51 Oil supply pipe 52 Oil supply pipe 53 Magnetic Processing Device 53a First Magnetic Processing Device 53b Second Magnetic Processing Device 53c Third Magnetic Processing Device 54 Storage Container 55 Magnetic Tank 56 Permanent Magnet 57 Ion Exchange Filter Device 57a First Ion Exchange Filter Device 57b Second Ion Exchange Filter Device 57c 1st 3 Ion exchange filter device 58 Container 59 Filter tank 60 Ion exchange filter

Claims (17)

In a compound production system for producing a compound used as a fuel for an internal combustion engine,
The compound production system purifies water supplied from a predetermined water source to produce pure water, and electrolyzes pure water purified by the pure water generator to generate hydrogen gas. A hydrogen gas first generator that generates high-concentration hydrogen ion water in which hydrogen ions are dissolved from the pure water, and negative electricity is applied to the high-concentration hydrogen ion water generated by the hydrogen gas first generator. A negative power source for generating high-concentration hydrogen ion water from which the positive charge is removed by combining the negative charge of the negative electricity and the positive charge contained in the high-concentration hydrogen ion water to remove the positive charge A predetermined fuel is added to the generator and the high-concentration hydrogen ion water from which the positive charge has been removed by the negative power source generator, and the high-concentration hydrogen ion water and the fuel are mixed and stirred. Compound production system, characterized by being formed from the stirring and mixing apparatus and a high-concentration hydrogen ion water and fuel by electron coupling making said compound.   In the compound production system, at least two or more hydrogen gas first generators are connected in series in a state where they are arranged on the upstream side and the downstream side, and at least two or more negative power source generators are connected to the upstream side. The compound production system according to claim 1, wherein the compound production system is connected in series in a state of being arranged on the downstream side.   The first hydrogen gas generator is made of a plurality of mesh electrodes having a predetermined area made of a titanium alloy, a plurality of mesh electrodes having a predetermined area made of an iridium oxide alloy, and a carbon nanotube. The compound according to claim 1 or 2, wherein any one of a plurality of mesh-shaped electrodes having a predetermined area is used to electrolyze the pure water by passing an electric current through the purified water. Manufacturing system.   The compound production system is installed between the hydrogen gas first generator and the negative power generator or downstream of the negative power generator, and is dissolved in the high-concentration hydrogen ion water by the magnetic force of a permanent magnet. Performing a magnetic treatment to remove oxygen ions to generate high-concentration hydrogen ion water from which oxygen ions have been removed, between the hydrogen gas first generator and the negative power generator, or Ion exchange that is installed downstream of the negative power generator and has an ion exchange filter that removes oxygen ions dissolved in the high-concentration hydrogen ion water, and generates high-concentration hydrogen ion water from which the oxygen ions have been removed. The compound manufacturing system according to any one of claims 1 to 3, comprising at least one of a filter device.   In the compound production system, at least two or more magnetic processing devices are connected in series in a state where they are arranged on the upstream side and the downstream side, and at least two or more ion exchange filter devices are connected to the upstream side and the downstream side. The compound production system according to claim 4, wherein the compound production system is connected in series in a state of being arranged in a column.   The compound production system is installed on the downstream side of the negative power generator, extracts a part of the high-concentration hydrogen ion water flowing out from the negative power generator, and electrolyzes the part of the high-concentration hydrogen ion water A hydrogen gas second generator that generates hydrogen gas and generates mist-like high-concentration hydrogen ion water in which the hydrogen ions are dissolved. In the compound production system, the hydrogen gas is generated by the hydrogen gas second generator. The compound manufacturing system according to claim 4 or 5, wherein mist-like high-concentration hydrogen ion water is supplied to the pure water.   The compound production system is installed on the downstream side of the magnetic processing device or the ion exchange filter device, extracts a part of high-concentration hydrogen ion water flowing out from the magnetic processing device or the ion exchange filter device, and A hydrogen gas second generator that generates hydrogen gas by electrolyzing high-concentration hydrogen ion water in a portion to generate mist-like high-concentration hydrogen ion water in which the hydrogen ions are dissolved. In the compound production system, The compound manufacturing system of Claim 4 or 5 which supplies the mist-like high concentration hydrogen ion water produced | generated by the said hydrogen gas 2nd generator to the said pure water.   The hydrogen gas second generator is made of a plurality of mesh electrodes having a predetermined area made of a titanium alloy, a plurality of mesh electrodes having a predetermined area made of an iridium oxide alloy, and a carbon nanotube. The high concentration hydrogen ion water is electrolyzed by applying an electric current to the partial high concentration hydrogen ion water using any one of a plurality of mesh electrodes having a predetermined area. Item 8. The compound production system according to Item 7.   The compound production system is installed on the upstream side of the first hydrogen gas generator, and generates hydrogen ions in pure water purified by the pure water generator using a mineral mainly composed of magnesium. The compound manufacturing system according to any one of claims 1 to 8, further comprising a hydrotreating apparatus that performs hydrotreating and generates hydrogen ion water in which the hydrogen ions are dissolved.   The compound manufacturing system according to claim 9, wherein in the compound manufacturing system, at least two or more hydroprocessing apparatuses are connected in series in a state of being arranged on the upstream side and the downstream side.   The mineral is drabite porous ceramic, and the hydrotreating apparatus contains a plurality of the drabite porous ceramics, and the pure water flows through the drabite porous ceramics so that the hydrogen ions are The compound manufacturing system according to claim 9 or 10, wherein dissolved hydrogen ion water is generated.   The compound production system according to any one of claims 1 to 11, wherein in the stirring and mixing device, the high-concentration hydrogen ion water and the fuel are stirred and mixed in a state of being pressurized to a predetermined pressure.   The compound production system according to any one of claims 1 to 12, wherein a redox potential of the high-concentration hydrogen ion water is -750 mv or less.   The fuel is light oil, and in the compound production system, the proportion of the light oil introduced into the stirring and mixing device is 60 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water flowing into the stirring and mixing device. The compound production system according to any one of claims 1 to 13, which is in a range.   The fuel is kerosene, and in the compound production system, the ratio of the kerosene charged into the stirring and mixing device is 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ionized water flowing into the stirring and mixing device. The compound production system according to any one of claims 1 to 14, which is in the range.   The fuel is heavy oil, and in the compound production system, the ratio of the heavy oil charged into the stirring and mixing device is 50 to 70% by weight with respect to 100% by weight of high-concentration hydrogen ion water flowing into the stirring and mixing device. The compound production system according to any one of claims 1 to 15, which is in the range. 2. The water source is at least one of a well, rain, a river, a lake, and a pond, and the water is at least one of a well water, a rain storage water, a river water, a lake water, and a pond water. The compound manufacturing system in any one of Claim thru | or 16.

Images