JP2009203456A - Device and method for generating water electrolytic gas mixed fuel - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a device and a method for generating water electrolytic gas mixed fuel, by mixing a water electrolytic gas generated by electrolyzing water in a basic electrolyte, with gasified petroleum fuel. <P>SOLUTION: This device 10 for generating the water electrolytic gas mixed fuel has a mixing vessel 11 for storing a liquid organic compound such as an alkane, an alcohol or an ether, and for mixing repeatedly the supplied bubble-like water electrolytic gas, with the gasified petroleum fuel, a water electrolytic gas supply means 12 for supplying, in a bubble-like state, the water electrolytic gas generated by the water electrolysis using the basic electrolyte, to the mixing vessel, a petroleum fuel supply means 13 for supplying the gasified petroleum fuel in a bubble state, to the mixing vessel, and a water electrolytic gas mixed fuel discharge means 14 for discharging the water electrolytic gas mixed fuel, to a fuel using device, and is provided further with an elevatable movable part 15 constituted into elevatable structure capable of elevating partitioning plates 51, 52, 53 formed with a plurality of micro pores of a degree not passing easily the bubbles of the water electrolytic gas and the gasified petroleum fuel. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a water electrolysis gas mixed fuel producing apparatus and production obtained by mixing a water electrolysis gas obtained by water electrolysis using a basic electrolyte and a gas fossil fuel such as liquefied natural gas or liquefied petroleum gas. Regarding the method.

It is a well-known fact that water (H ₂ O) is ionized in a basic potassium hydroxide (KOH) aqueous solution to generate hydroxide ions OH ⁻ and hydrogen ions H ⁺ . Here, the hydroxide ion OH ⁻ is also called an anion in the sense that it moves from the cathode (cathode) side to the anode (anode) side, and the hydrogen ion H ⁺ is the anode (anode) on the contrary. It is also called a cation because it is an ion that moves from the side to the cathode (cathode) side. This hydrogen ion H ⁺ forms a covalent bond with the mixed water molecule H ₂ O and becomes an “oxonium ion (H ₃ O ⁺ )”. This means that in an environment where water and hydrogen ions coexist, that is, in the water electrolysis cell, many exist as “oxonium ions (H ₃ O ⁺ )” by covalent bonds. A number of apparatuses for generating water electrolysis gas, also called hydrogen-oxygen gas, by water electrolysis have been disclosed. The present invention uses a water electrolysis gas obtained by water electrolysis in a basic electrolyte.

  As a prior art in which water and fossil fuel are mixed and burned in a special state, Patent Document 1 mixes water with water vapor and mist fossil fuel, and connects pipes for supplying the mixed fuel. An improved fossil fuel combustion apparatus is disclosed. In this pipe, a passage for passing water vapor is formed in the water vapor manifold, and a mist of kerosene is introduced into the water vapor passage. Moreover, the first and second nozzle support pipes are formed in such a water vapor manifold. A gas fossil fuel combustion apparatus is disclosed in which a gas manifold is attached to the front of the water vapor manifold, and a first gas nozzle and a second gas nozzle for injecting brown gas are provided. The combustion apparatus according to this prior art attempts to achieve proper combustion by mixing water vapor with atomized kerosene and mixing with brown gas in a gas manifold.

  Patent Document 2 discloses a combustion method and combustion apparatus for a water / fossil fuel mixed emulsion. According to this document, water (fossil fuel mixed emulsion) is irradiated with microwaves (ultra-short wave) to raise the temperature and vaporize. The water / fossil fuel mixed gas thus heated and vaporized is supplied to the burner and burned. The burner is preferably supplied with a high-temperature gas heated to brown gas combustion, and as a result, a high temperature of about 2000 ° C. can be obtained.

  Patent Document 3 discloses a brown gas combustion burner that burns brown gas safely and reliably. The burner is formed with a burner body in which a brown gas inlet and a gas injection port communicate with each other, and at least one or more flashback prevention means is provided inside the brown gas flow path of the burner body. The structure which raises is disclosed. Each of these prior documents is intended to burn a gas obtained by adding water to water vapor or brown gas obtained from water to the fuel. A method or apparatus for directing and burning is disclosed.

Patent Document 4 is a device that supplies brown gas to a mixing tank containing a liquid volatile organic compound therein, and mixes the gaseous organic compound vaporized from the liquid volatile organic compound with the brown gas. Provided with a partition wall formed with pores for ventilation that do not allow Brown gas bubbles to pass through the inside of the tank, a closed cell aggregate is formed on the lower surface of the partition wall, and further, the brown gas bubbles are supplied to the closed cell aggregate Then, an apparatus and a manufacturing method for manufacturing mixed brown gas by adsorption and growth are disclosed. In this invention, the gaseous organic compound vaporized from the liquid volatile organic compound in the mixing tank and the brown gas are mixed, and the partition provided inside the mixing tank is not a movable structure, Means for stopping and starting the supply of gas, combustible organic compound gas, and the like to the mixing tank is not disclosed, and is completely different in configuration from the present invention.
Japanese Patent Laid-Open No. 2002-5414 JP-A-10-267260 JP 2003-207107 A JP 2005-320416 A

  The subject of this invention is providing the apparatus and production | generation method of producing | generating a water electrolysis gas mixed fuel by mixing the water electrolysis gas produced | generated by the water electrolysis in basic electrolyte solution, and gaseous fossil fuel. The inventors have conducted various studies on a device that mixes water electrolysis gas and gaseous fossil fuel, and as a result, carbon dioxide emissions are reduced and consumption of gaseous fossil fuel as a raw material can be greatly reduced. This has led to the development of a device that can produce fuel that can continuously obtain powerful thermal power.

  As shown in FIGS. 1 and 2, the invention described in claim 1 contains a liquid L selected from an organic compound such as an alkane-based, alcohol-based, or ether-based substance inside, and is supplied in the form of a bubble. A mixing tank 11 that repeatedly performs the mixing of the water electrolysis gas and the gas fossil fuel, and a water electrolysis gas supply that supplies the water electrolysis gas generated by water electrolysis using a basic electrolyte to the mixing tank in the form of bubbles. Fuel means 12, fossil fuel supply means 13 for supplying gas fossil fuel in the form of bubbles to the mixing tank, and water electrolysis gas mixed fuel produced by repeatedly performing mixing of the water electrolysis gas and gas fossil fuel In the water electrolysis gas mixed fuel generating device having the water electrolysis gas mixed fuel discharging means 14 for discharging to the use device 60, a plurality of pores to such an extent that bubbles of the water electrolysis gas and the fossil fuel cannot easily pass therethrough are formed. Formation A plurality of partition plates 51 that are immersed in the liquid L accommodated in the mixing tank and are installed in the horizontal direction with the outer peripheral surface of the partition plate approaching the inner wall of the mixing tank, The up-and-down movable unit 15 configured to be movable up and down with 52 and 53 attached thereto, the stop or start of the supply to the mixing tank of the water electrolysis gas and / or the gas fossil fuel, the supply amount, and the predetermined component ratio And a control device 20 for controlling the water-electrolyzed gas mixed fuel generation device.

  The invention according to claim 2 is a water electrolysis gas mixed fuel in which the liquid L of an organic compound such as an alkane-based, alcohol-based, or ether-based material is one selected from gasoline, ethanol, methyl alcohol, and dimethyl ether. The invention according to claim 3 is a water electrolysis gas in which the gasified fossil fuel is one of gasified fossil fuel selected from liquefied petroleum gas (LPG), liquefied natural gas (LNG), and coal dry distillation gas. It is a mixed fuel generating device. According to a fourth aspect of the present invention, the water electrolysis gas mixed fuel generated by the water electrolysis gas mixed fuel generator vaporizes from the liquid L of an organic compound such as an alkane-based, alcohol-based, or ether-based material. It is the generating apparatus of the water electrolysis gas mixed fuel containing this.

  According to a fifth aspect of the present invention, the partition plates 51, 52 and 53 attached to the elevating movable part 15 are formed in three stages, and the lowermost partition plate 51 has a thickness of 0.5 to 2.5 mm, preferably Is made of stainless steel having a pore diameter of about 1 to 2 mm and a pore diameter of 0.5 to 3.5 mm, preferably about 1 to 3 mm, and the upper partition plates 52 and 53 have a pore diameter of 0.2 to 1.5 mm. The water-electrolyzed gas mixed fuel generator is preferably a flat mesh structure of about 0.3 to 1 mm. Moreover, the partition plates 51, 52, and 53 can be made of resin, and the resin partition plate can have a thickness of about 10 to 15 mm and a pore diameter of about 3 to 10 mm. Note that the shape of the pores formed in the partition plate can be tapered upward.

  According to a sixth aspect of the present invention, the control means 20 is configured such that a large number of bubbles of the water electrolysis gas and gas fossil fuel gather on the lower surface side of the partition plate and the movement to the upper layer is stagnant, or the bubbles The displacement of the ascending / descending movable unit 15 to which the partition plate is attached, which is caused by moving through the pores and moving to the upper layer, is detected, and the supply of water electrolysis gas and gas fossil fuel into the mixing tank is detected. It is a water electrolyzed gas mixed fuel generating device that controls stop or start (restart).

  In the seventh aspect of the present invention, the control means 20 detects a change in the internal pressure of the mixing tank 11 and controls stop or start (resumption) of supply of water electrolysis gas and gas fossil fuel into the mixing tank. In the invention according to claim 8, the control means 20 is configured such that the internal pressure of the mixing tank is a pressure set as a condition for stopping the supply of the fossil fuel into the mixing tank. Detects that the same pressure has been reached, stops supplying water electrolysis gas into the mixing tank, detects that the internal pressure of the mixing tank has dropped below the set pressure, and supplies water electrolysis gas into the mixing tank This is a water electrolysis gas mixed fuel generation device that is controlled to start (restart).

  In the invention according to claim 9, as shown in FIG. 3, the water electrolysis gas generator 30 supplied to the water electrolysis gas supply means 12 has an electrolyte inlet 31 on the bottom side, An electrolytic cell having an extraction port 35 for taking out a mixture of electrolytic solution and product gas on the side, the anode plate 32 disposed on the bottom side in the electrolytic cell, and the top side in the electrolytic cell Water provided with the disposed cathode plate 33 and electrolyte swirl flow means 34 without electrical connection for allowing the alkaline electrolyte to flow while swirling in the direction from the anode plate toward the cathode plate A mixture of water electrolytic gas and electrolytic solution taken out from the electrolytic cell 300 for electrolytic gas generation and the outlet 35 at the upper end of the electrolytic cell is introduced to separate the gas component of the water electrolytic gas from the electrolytic solution. The gas component is taken out and the electrolyte component remains. Water electrolytic gas-electrolyte separation tank 301 for forcibly cooling, electrolytic solution forced cooling means 302 for forcibly cooling the electrolytic solution remaining in the separation tank, and electrolysis for circulating the electrolytic solution to the electrolytic tank side It is a water electrolysis gas mixed fuel generation device which is a water electrolysis gas generation device comprising a liquid circulation means 303.

  In the invention according to claim 10, as shown in FIG. 4, the electrolyte swirl flow means 34 disposed between the anode plate 32 and the cathode plate 33 in the electrolytic cell 300 includes a required number of sheets. The metal plates 34-1 to 34-n have 2 to 6 flow openings 47 which are perforated symmetrically off the outer periphery from the respective centers, and these flow openings are sequentially displaced by a predetermined angle. It is a water-electrolyzed gas mixed fuel generating device having a structure in which an electrolytic solution is allowed to flow while being accompanied by a swirling flow.

The invention according to claim 11 introduces water electrolysis gas generated by water electrolysis using a basic electrolyte and gas fossil fuel in the form of bubbles, and from organic compounds such as alkane-based, alcohol-based, and ether-based materials. In the mixing tank 11 containing the selected liquid L inside, the mixing is repeatedly performed so that the introduced water electrolysis gas and the fossil fuel are uniformly mixed,
A partition plate in which a plurality of pores are formed so that bubbles of the water electrolysis gas and gas fossil fuel cannot easily pass through the partition plate, and the partition plate is immersed in the liquid L accommodated in the mixing tank. The water electrolysis gas comprises an elevating movable part 15 configured to be movable up and down to which a plurality of partition plates 51, 52, 53 installed in a horizontal direction with an outer peripheral surface approaching the inner wall of the mixing tank are attached. And a large number of bubbles of gas fossil fuel are gathered on the lower surface side of the partition plate and the movement to the upper layer stagnate, or the partition plate generated by the bubbles passing through the pores and moving to the upper layer is attached. Detecting the displacement of the rising and lowering of the movable movable unit 15 to stop or start (restart) the supply of water electrolysis gas and gas fossil fuel into the mixing tank, control the supply amount, and the predetermined component ratio; Mixing of electrolytic gas and gas fossil fuel continues. And generating the executed electrolytic gas mixture fuel, characterized in that it is a method of generating electrolytic gas mixture fuel.

  The invention according to claim 12 is the production of the water electrolysis gas mixed fuel in which the control of stopping or starting (restarting) the supply of the water electrolysis gas and the gas fossil fuel into the mixing tank is performed by detecting the change in the internal pressure of the mixing tank. According to a thirteenth aspect of the present invention, the control for stopping the supply of the water electrolysis gas into the mixing tank is a mixing in which the internal pressure of the mixing tank is set as a supply stop condition for the fossil fuel mixing tank. It is performed by detecting that the internal pressure of the tank has reached the same level, and the control for starting (resuming) the supply of water electrolysis gas into the mixing tank detects that the internal pressure of the mixing tank has dropped below the set internal pressure. It is a production method of a water electrolysis gas mixed fuel performed.

  According to the water electrolysis gas mixed fuel generating apparatus according to the present invention, the water electrolysis gas obtained by water electrolysis in the basic electrolyte and the gas fossil fuel are introduced into the bottom of the mixing tank 11 while being pressurized, In the presence of a liquid selected from organic compounds such as alkane-based, alcohol-based, and ether-based substances contained in the tank, the mixing of the bubbly water electrolysis gas and the raw gas fossil fuel is repeatedly performed. A water electrolysis gas mixed fuel is produced. The water electrolysis gas and the fossil fuel are introduced into the mixing tank 11 in the form of bubbles, and mixed and assembled on the lower surface side of the partition plates 51, 52, 53 in which many pores are formed so that these bubbles cannot easily pass through. Execute. This partition plate is integrally attached to an elevating movable part 15 configured to be movable up and down in the mixing tank, and is immersed in the liquid accommodated in the mixing tank and its outer peripheral surface approaches the mixing tank inner wall. In this state, they are arranged in the horizontal direction.

  In the present invention, since the partition plate is formed with a large number of pores to the extent that the water electrolysis gas and the gas of the fossil fuel cannot easily pass through, the bubbles introduced under pressure at the bottom of the mixing tank 11 A large number of aggregates are formed on the lower surface side of the partition plate to form an aggregate, and the movement to the upper layer is stagnated. As a result, the internal pressure of the mixing tank is increased, and therefore the movable movable portion 15 to which the partition plate is attached rises. As the air bubble aggregate is destroyed and the air bubbles pass through the fine holes of the partition plate and move to the upper layer, the elevating movable unit 15 is lowered. Such a displacement of the ascending / descending movable part 15 is detected by a touch sensor or the like, or a change in the internal pressure of the mixing tank is detected by a pressure sensor, and the raising / lowering movable part 15 is raised or the inside of the mixing tank is When the pressure becomes high, the water electrolysis gas generator is turned off to stop the supply of water electrolysis gas, and the throttle valve is closed to stop the supply of gas fossil fuel into the mixing tank. ing.

  With such a configuration, when the water electrolysis gas mixed fuel produced by the present invention is burned by a heating burner that burns conventional liquefied natural gas (LNG), liquefied petroleum gas (LPG) or the like, only LPG is burned. It has been confirmed that the amount of LPG consumed for obtaining the same amount of heat is about 40%, which is significantly reduced. In addition, since the supply of water electrolysis gas is stopped under certain conditions, the power consumption for operating the water electrolysis gas generator is also reduced. The water electrolysis gas mixed fuel produced in this way and taken out from the discharge means 14 is reformed so as to obtain almost complete combustion.

  By mixing the water electrolysis gas and the gas fossil fuel as described above, the combustion efficiency is greatly improved, and the consumption of fossil fuel required for obtaining the required heat quantity can be greatly reduced. Moreover, regarding the water electrolysis gas obtained by water electrolysis in the above basic electrolyte, the water electrolysis gas produced by the name “water electrolysis gas generator” disclosed in Japanese Patent Application No. 2008-277756 relating to the present applicant. Can be advantageously used. According to the water electrolysis gas generator, water electrolysis gas can be efficiently and continuously generated and introduced into the mixing tank 11 through the water electrolysis gas supply means 12 under pressure. Since this water electrolysis gas is basically generated by electrolysis of water, it is clear that it is a material that is extremely advantageous in terms of quantity and economy.

  By using water electrolysis gas obtained by electrolysis of water, which is an inexpensive and abundant material, the combustion efficiency of gaseous hydrocarbons and other carbon-containing substances can be improved. It is also advantageous from the viewpoint of effective use of energy resources that water-electrolyzed gas mixed fuel is produced by mixing water-electrolyzed gas with gas fossil fuel and exhibits the effect of increasing the amount of heat.

  According to the water electrolysis gas mixed fuel taken out according to the present invention, a powerful combustion reaction is possible as described above. Further, in the present invention, the water electrolysis gas mixed fuel contains a gas evaporating from a liquid of an organic compound such as an alkane-based, alcohol-based, or ether-based substance contained in the mixing tank, so that a more powerful and active combustion reaction Is possible. The use of such a combustion reaction is not limited to a simple burner such as a heating device or a heater, but is used as a gaseous fuel in a wide range of combustion devices such as internal combustion engines, gas turbines, jet engines, and many other heat engines. It can also be used as fuel for these various heat engines.

  According to the present invention, by mixing the water electrolysis gas and an appropriate kind of gas fossil fuel, the combustion reaction of the gas fossil fuel becomes active and a strong thermal power can be obtained. As a result, when the same amount of heat is obtained, the consumption of the original gas fossil fuel alone is reduced by about 60% compared with the conventional combustion method using oxygen in the atmosphere. Therefore, the amount of air required for combustion to obtain the same amount of heat is also reduced, so that the thermal efficiency is improved and the generated carbon dioxide emission is also reduced proportionally. Naturally, it is effective as a measure against global warming in addition to saving and effective use of fossil fuels with limited reserves. Moreover, since the discharge amount of sulfur oxide (SOx) and nitrogen oxide (NOx) is greatly reduced, it is extremely effective as an environmental measure.

  Next, a water electrolyzed gas mixed fuel generating device and method according to the present invention will be disclosed with reference to the accompanying drawings. FIG. 1 (A) is a schematic cross-sectional view for explaining a water electrolysis gas mixed fuel generating apparatus according to the present invention, and FIG. 1 (B) is a cross-sectional view taken along line AA in FIG. 1 (A). . FIG. 2 is a block diagram showing a water electrolysis gas mixed fuel generating device and related peripheral devices according to the present invention. As shown in the figure, a water electrolysis gas mixed fuel generation apparatus 10 according to the present invention contains a liquid L selected from an organic compound such as an alkane-based, alcohol-based, or ether-based substance inside, and is introduced from the bottom. The mixing tank 11 that repeatedly executes mixing of the bubbly water electrolysis gas and the gas fossil fuel, and the water electrolysis gas that supplies water electrolysis gas generated by water electrolysis using a basic electrolyte to the mixing tank Supply means 12, fossil fuel supply means 13 for supplying gas fossil fuel to the mixing tank, and water electrolyte gas mixed fuel generated by repeatedly mixing the water electrolysis gas and gas fossil fuel is discharged to the fuel use device 60. The water electrolysis gas mixed fuel discharging means 14 is configured.

  The water electrolysis gas mixed fuel generating device 10 includes a water electrolysis device 30 as water electrolysis gas generating means for generating a water electrolysis gas, which will be described later, and a liquefied petroleum gas as a device for supplying gaseous fossil fuel such as liquefied petroleum gas. A gas cylinder 40 such as is connected. The generated water electrolysis gas mixed fuel gas is supplied to a combustion burner or other fuel use device 60. Control means 20 for controlling the operation of each component of the apparatus according to the present invention, such as stopping or starting the supply of water electrolysis gas and / or gas fossil fuel to the mixing tank, controlling the supply amount, the predetermined component ratio, and the like. Is provided.

  Inside the mixing tank 11, an elevating movable part 15 configured to be movable up and down in the mixing tank is disposed, and the elevating movable part 15 has a peripheral surface on the upper end surface of the outer peripheral surface outer frame part 16. A suspension part 54 detachably disposed at the end, a partition plate 53 fixed by the suspension part 54 and four connecting rods 57 made of stainless steel, and a partition plate 52 fixed by the partition plate 53 and the connection rod 56. The partition plate 51 fixed by the partition plate 52 and the connecting rod 55 is fixed and attached integrally. A gap S of about 5 to 10 mm is formed between the upper surface of the suspending portion 54 and the upper surface outer frame portion 17 in order for the elevating movable portion 15 to perform the raising and lowering operations due to the change in the internal pressure of the mixing tank. Yes.

  The hanging portion 54 is formed in a circular flat plate shape having an opening 58 for guiding the water electrolyzed gas mixed fuel to the water electrolyzed gas mixed fuel discharging means 14 at the center. In addition, since the cylindrical mixing vessel 11 is used in the present embodiment, the hanging portion 54 and partition plates 51, 52, and 53 described later are circular flat plates, but the shape of the hanging portion and the partition plate is The shape is not limited to a circular flat plate shape, and these shapes can be polygonal shapes such as pentagons, hexagons, and heptagons according to the shape of the mixing tank. Of course, the shape of the mixing vessel 11 can be various polygonal shapes.

  The partition plates 51, 52, 53 attached to the up-and-down movable unit 15 are formed with a plurality of pores to the extent that water electrolysis gas and gas fossil fuel bubbles cannot easily pass through, and the liquid contained in the mixing tank And is installed in the horizontal direction with the outer peripheral surface of the partition plate approaching the inner wall of the mixing tank. The lowermost partition plate 51 has a thickness of 0.5 to 2.5 mm, preferably about 1 to 2 mm, a pore diameter of 0.5 to 3.5 mm, preferably about 1 to 3 mm, and is made of stainless steel. Or it can be made from resin. The partition plates 52 and 53 thereabove can be a flat mesh structure made of stainless steel or resin having a pore diameter of 0.2 to 1.5 mm, preferably about 0.3 to 1 mm. Further, when the partition plates 51, 52, and 53 are made of resin, the partition plate can have a thickness of about 10 to 15 mm and a pore diameter of about 3 to 10 mm. The shape can also be tapered upward.

  The partition plates in which a large number of pores are formed in this way are installed in a plurality of stages because the bubbly water electrolysis gas introduced to ensure reliable and uniform mixing between the water electrolysis gas and the gas fossil fuel. It is intended to adjust the residence time and pressure of gas fossil fuel. In this embodiment, the partition plates to be attached to the elevating movable unit 15 are formed in three stages, but the number of partition plates is not limited to this, and 1 according to the diameter and density of the formed pores. It can be a plurality of stages. In this embodiment, the movable structure of the elevating movable part is arranged so that the outer peripheral end surface of the hanging part 54 can be detached from the upper end part of the outer peripheral outer frame part 16. The connecting portion of the connecting rod 57 that connects and fixes the connecting plate 57 to the partition plate 53 may have a structure in which the lower end portion is used as a stopper and the connecting rod insertion portion of the partition plate is opened so as to be able to move up and down.

  Moreover, it is comprised so that the space | interval of each partition plate 51,52,53 attached to the raising / lowering movable part 15 can be adjusted according to the production conditions of the gas fossil fuel used for this apparatus, or a water electrolysis gas mixed fuel. can do. In this interval adjustment, connecting rods of various lengths prepared in advance are used as connecting rods having a desired length, or the connecting rods connecting the partition plates are attached with screws so that the desired intervals are obtained by adjusting the screws. This can be done by setting it to a predetermined length. The diameter and density of the pores formed in the partition plate, as well as the spacing and arrangement of the partition plates, the type of liquid such as alkane, alcohol, and ether substances filled in the tank, viscosity, volume, temperature, etc. In addition, it is possible to make adjustments so that a desired mixing speed and yield can be obtained in consideration of the type of gas fossil fuel, the supply amount, the scale of the apparatus, the generation amount of the water electrolysis gas mixed fuel, and the like.

  The mixing tank 11 is filled with a liquid L selected from organic compounds such as alkane-based, alcohol-based, and ether-based materials to the extent that it exceeds the uppermost partition plate 53. Here, as a liquid of an organic compound such as an alkane-based, alcohol-based, or ether-based material, for example, gasoline, ethanol, methyl alcohol, dimethyl ether, kerosene, or the like can be used. As gas fossil fuel supplied from the fossil fuel supply means 13, liquefied petroleum gas (LPG), liquefied natural gas (LNG), coal dry distillation gas, etc. can be used.

  Further, the water electrolysis gas mixed fuel produced by the apparatus according to the present invention contains a gas that evaporates from a liquid selected from organic compounds such as alkane-based, alcohol-based, and ether-based substances contained in the mixing tank. The vaporized gas can be used as a combustion aid for the water-electrolyzed gas mixed fuel, thereby enabling a more powerful and active combustion reaction. In this case, it is necessary to appropriately replenish the liquid L stored in the mixing tank.

  The water electrolysis gas and the gas fossil fuel introduced into the mixing tank from the water electrolysis gas supply means 12 and the fossil fuel supply means 13 are selected from organic compounds such as alkane-based, alcohol-based, and ether-based substances filled in the mixing tank. It is necessary to introduce a pressure opposite to the liquid pressure of the liquid, and a pressure injection of about 0.05 to 0.2 MPa, preferably about 0.08 to 0.15 MPa is performed. The water electrolysis gas supply means 12 and the fossil fuel supply means 13 are provided with check valves 102 and 103, respectively, in which the liquid filled in the mixing tank is transferred from the mixing tank to the water electrolysis gas. This prevents backflow to the fossil fuel supply device 40 such as the generation supply device 30 and the gas cylinder, and reliably prevents backflow when the inside of the mixing tank becomes high pressure.

  The apparatus according to the present invention includes control means 20 for controlling the stop or start of the supply of water electrolysis gas and / or gas fossil fuel to the mixing tank, the supply amount, the predetermined component ratio, and the like (see FIG. 2). The control means 20 is movable up and down to which a partition plate is attached, which is generated when a large number of bubbles of water electrolysis gas and gas fossil fuel gather on the lower surface side of the partition plate to form a bubble aggregate and the movement to the upper layer is stagnant. The displacement of the rising of the unit 15 is detected by a touch sensor or the like, and the supply of the water electrolysis gas and the gas fossil fuel from the water electrolysis gas generator 30 and the gas fossil fuel supply device 40 to the mixing tank is stopped. To do. On the other hand, when the bubble assembly is broken and the bubbles pass through the pores and move to the upper layer, the lowering movement of the elevating movable unit 15 is detected, and the water electrolytic gas and the fossil fuel are mixed into the mixing tank. Control to start or restart (restart) the supply.

  Further, the control means 20 detects a change in the internal pressure of the mixing tank caused by the movement of the bubbles to the upper layer or the movement of the bubbles to the upper layer by a pressure sensor, so that water electrolysis gas and gas fossil It can be controlled to stop or start (restart) the supply of fuel into the mixing tank. When the control means 20 detects that the internal pressure of the mixing tank has reached the same pressure as the pressure preset as the supply stop condition for the gas fossil fuel mixing tank, the control means 20 supplies the water electrolysis gas to the mixing tank. The supply can be controlled to be stopped, and when it is detected that the internal pressure of the mixing tank is lower than the set pressure, the supply of water electrolysis gas into the mixing tank can be started (restarted).

  Here, in stopping / starting (restarting) the supply of the water electrolysis gas into the mixing tank, it is performed by 0N / OFF switching control of the activation power source of the water electrolysis gas generator described later, and into the mixing tank of the gas fossil fuel. In stopping / starting (resuming) the supply, a throttle valve is provided in a gas cylinder 40 such as liquefied petroleum gas, and the throttle valve is controlled to be opened and closed. A control device for controlling the overall operation of each of these constituent elements is provided, but details are omitted because those skilled in the art can easily configure the existing control technology.

  FIG. 3 is a block diagram showing a basic configuration example of a water electrolysis gas generator for generating water electrolysis gas used in the water electrolysis gas mixed fuel generation apparatus according to the present invention, and FIG. 4 is a water electrolysis gas. It is a figure which shows the structural example of the electrolysis tank for water electrolysis gas production | generation of a generator. As shown in the figure, a water electrolysis gas generator 30 used in the present invention includes a water electrolysis gas generating electrolysis tank 300, a water electrolysis gas-electrolyte separation tank 301, an electrolysis solution forced cooling means 302, and an electrolysis solution circulation means. 303. In the electrolytic solution circulation system 303, a line filter 38 for impurity filtration, an electrolytic solution discharge port 39 for extracting the electrolytic solution in the system, and the like are appropriately arranged according to the illustrated portion or the configuration example of the same device. It is desirable.

  The electrolytic cell 300 includes an electrolytic solution inlet 31 at the bottom of the electrolytic cell, an anode plate 32 at the bottom of the electrolytic cell, and a cathode plate 33 at the top, and serves as an electrolyte swirl flow means 34 between the two electrodes. A required number of metal plates 34-1 to n are arranged at predetermined intervals. Stainless steel 304 or stainless steel 316 can be used for the anode and the cathode. As will be described later, each of the metal plate groups 34 is not electrically connected to both electrodes and other parts, and is fixedly supported by a cylindrical insulator 37 formed of various plastics. In addition, the individual metal plates are not electrically connected to each other, but a potential difference corresponding to a potential gradient that is inevitably formed from the anode side to the cathode side by the electrolyte layer filled between the anode and the cathode. It has a corresponding potential and acts so that the swirling flow action of the intervening electrolyte is uniform.

  In the present invention, it is possible to suppress the rise in temperature in the electrolytic cell by forced circulation of the electrolytic solution by the electrolytic solution circulation device and swirling flow of the electrolytic solution by the metal plate group as swirl flow means. The outer frame body that fixes and supports the plate group can be made of plastic such as vinyl chloride. Thereby, the manufacturing cost of an electrolytic cell can be reduced significantly. Further, the outside of the electrolytic cell is surrounded by an insulator, so that leakage is avoided. It is convenient to set the intervals between the metal plates 34-1 to 34-n so that, for example, the potential difference between them is 1.8 [V]. Water electrolysis is performed in a process in which the electrolytic solution swirls between the required number of metal plate groups 34 and the cathode through the anode, and water electrolysis gas is generated. By arranging a large number of these metal plates, it is possible to generate a large amount of water electrolysis gas from the electrolytic cell while accelerating it. The mixture of the water electrolysis gas and the electrolytic solution is taken out from the upper outlet 35.

  FIG. 5 shows an example of a single body constituting the metal plate group 34 in which a required number of, for example, about 10 to 100 or more sheets are arranged at predetermined intervals between the anode and the cathode in the electrolytic cell 300. It is. In this embodiment, the shape of the metal plate is circular as shown in FIG. 5, but may be a polygon such as a pentagon, a hexagon, a heptagon,. In this embodiment, which is formed as a disc, four electrolyte solution passage openings 47 are formed by drilling at a point symmetric with respect to the center point C. In addition, since the circular metal plate is used in this embodiment, the outer frame body that fixes and supports these metal plate groups is cylindrical, but the shape of the outer frame body that fixes and supports these metal plate groups is cylindrical. The shape of the metal plate is not limited to a polygonal shape, and when the shape of the metal plate is a polygon such as a pentagon, a hexagon, or a heptagon, a polygonal cylindrical body may be formed in accordance with the shape of the metal plate. it can.

  The electrolyte passage opening 47 formed in the single body allows water electrolysis gas and electrolyte to flow from the anode side to the cathode side. When assembling and fixing such a metal disk, the opening is provided. Positioning is performed so that 47 is sequentially displaced by a predetermined angle, for example, 15 degrees as shown in [1] to [6] in FIG. As a result, the opening of the next-stage metal plate disposed at a predetermined interval above the opening of the metal plate adjacent to the anode is displaced, for example, 15 degrees counterclockwise, and the opening of the metal plate above it is Further, an appropriate number of metal plates selected from the required number, from several tens to several hundreds, while being sequentially displaced at an appropriate angle such as 15 degrees, are fixedly supported by the cylindrical insulator. The displacement angle of the opening is not limited to 15 degrees.

  The DC voltage applied between the anode plate and the cathode plate varies depending on the number of metal plate groups interposed in the middle, but is selected so that the potential difference between the individual metal plates is approximately 1.8 [V]. It is desirable. When attention is paid to the openings 47 corresponding to each of these metal plates, they are gradually displaced from the anode side to the cathode side by a predetermined angle, for example, 15 degrees, and the passing electrolyte solution is aligned in a spiral shape. . The electrolyte flowing in the direction from the anode to the cathode in the metal plate group arranged so that the openings are sequentially displaced by a predetermined angle in this way follows the flow path determined by the number of metal plate groups arranged and the displacement angle. An upward flow is formed with a turn. As a result, the electrolytic solution flows while receiving regular agitation, so that the electrolytic reaction is promoted, and an improvement in the production yield of the water electrolysis gas can be expected.

  In addition, since the opening of such a metal plate also exhibits the effect which accelerates | stimulates the raise of the water electrolysis gas generated with progress of an electrolysis reaction, it is convenient to provide about 4-6 pieces. In addition, an electrolytic solution supply port 36 with a valve is provided at the upper end of the electrolytic cell 300 to supply a new electrolytic solution. The electrolytic solution replenishment port may be attached by connecting a branch valve to another part, for example, a pipe connected to the electrolyte solution introduction port 31 at the lower end, and replenishing via the branch valve. .

  A mixture of the water electrolysis gas and the electrolytic solution taken out from the electrolytic bath 300 is introduced from the inlet 41 on the bottom side. The introduction port 41 protrudes into the tank from the bottom of the separation tank 301 and is provided with a large number of fine holes or a discharge port formed of a porous material, through which water electrolysis gas and electrolysis are formed. The mixture with the liquid is discharged into the tank. By comprising in this way, the difference in the resistance at the time of a gas component passage and the resistance at the time of electrolyte solution passage will promote dispersion | distribution of a gas component, and favorable gas-liquid separation will be promoted. The gas component of the water electrolysis gas thus separated into gas and liquid is pressurized into the mixing tank 11 through the water electrolysis gas supply means 12 from the gas outlet 45 disposed at the upper end of the separation tank. be introduced.

  As a result of such gas-liquid separation, the electrolyte remaining in the separation tank is taken out from the electrolyte outlet 42 provided at the bottom of the separation tank, and a part thereof is transferred to the electrolyte forced cooling device 302. It is cooled to an appropriate temperature, and then returned to the separation tank through the cooling electrolyte inlet 43 provided at the bottom of the separation tank. In this case, the temperature of the electrolytic solution in the electrolytic cell is preferably about 18 ° C. to 25 ° C., although it varies depending on the outside air temperature, the generated gas yield, and the like. As for the working temperature, if the temperature is too low, the reaction becomes unstable. On the other hand, if the temperature is too high, the electrolytic reaction efficiency is lowered. Therefore, it is desirable to maintain the temperature range as described above.

  The remaining electrolytic solution that has not been transferred to the electrolytic solution forced cooling device 302 is circulated through the electrolytic cell by the electrolytic solution circulation device 303. In this case, regarding the proportion of the electrolyte to be transferred to the electrolyte forced cooling device or directly refluxed to the electrolytic cell, the required control is taken into account the operating environment, for example, the outside air temperature, the temperature of the electrolyte, the operating time, etc. It is desirable to implement the optimal increase / decrease adjustment by using the apparatus. In such a configuration, as shown in FIG. 3, one electrolytic solution outlet is provided at the bottom of the separation tank, and it is branched into a flow path that circulates to the electrolytic solution forced transfer device and the electrolytic tank in the middle of the pipe. This is applied when configured as described above.

  In addition, an electrolyte outlet is separately provided at the bottom of the separation tank for circulation of the electrolytic tank, and the electrolytic solution cooled to an appropriate temperature remaining in the separation tank is discharged from the electrolyte outlet by an electrolyte circulation pump. On the other hand, the electrolytic solution taken out from a separately provided outlet is circulated to the separation tank via the cooling electrolyte inlet by a circulation pump 44 provided independently of the electrolytic forced cooling device. It may be configured.

  The water electrolysis gas generator configured as described above generates water electrolysis gas efficiently and continuously, and the generated water electrolysis gas is supplied from the gas outlet 45 disposed at the upper end of the separation tank. Pressure is introduced into the mixing tank 11 through the means 12. The water electrolysis gas and the gas fossil fuel introduced under pressure from the water electrolysis gas generator 30 and the gas cylinder 40 are supplied into the mixing tank in the form of a number of bubbles, and these bubbles are first on the lower surface side of the lowermost partition plate 51. The bubbles are aggregated to form a bubble aggregate, and mixing is continuously performed. When a predetermined time elapses, the bubble aggregate is broken to become fine bubbles, passes through the pores formed in the partition plate 51, and bubbles gather on the lower surface side of the partition plate 52 to perform mixing. Thereafter, the bubble aggregate is broken to become fine bubbles, and gathers on the lower surface side of the partition plate 53 in the same manner to perform mixing. Thus, by repeatedly performing the collection and mixing, the water electrolysis gas mixed fuel is generated and supplied from the water electrolysis gas mixed fuel discharging means 14 to the fuel use device 60.

  FIG. 6 is a photograph of the arrangement state of the entire demonstration device for confirming the performance of the water electrolysis gas mixed fuel obtained by the present invention, and FIG. 7 is a diagram of a flame generated from the combustion burner in the demonstration device. This is a picture of the situation. These photographs were taken by Toshihiko Sato, who lives in 1544-1 Moro Hongo, Moroyama-cho, Iruma-gun, Saitama Prefecture. The date of photography is January 18, 2008. 6 and 7, a combustion burner 60 that blows out a flame, a water-electrolyzed gas mixed fuel generating device 10, a water-electrolytic gas generating device 30, and a control device 20 are shown in order from the left side. In addition, since the LPG cylinder 40 as a fossil fuel supply apparatus used here is installed outdoors, it is not shown in these drawings.

  The configuration of the water electrolysis gas mixed fuel generation device in the demonstration apparatus as described above is such that gasoline is filled in the mixing tank, and the suspension part and the three-stage partition plate are fixed in the mixing tank by a stainless connecting rod. Ascending and descending movable parts configured in a movable structure attached as described above are disposed, and the bottom partition plate is formed of a stainless steel plate having a thickness of about 1.5 mm with a pore having a diameter of about 1.5 mm, The upper partition plate was formed by forming pores having a diameter of about 0.5 mm in a stainless steel mesh structure.

An experiment was attempted by supplying water electrolysis gas generated by the water electrolysis gas generator from the bottom of the mixing tank of the demonstration apparatus having such a configuration and LP gas from an LP gas cylinder having a set pressure of about 0.1 MPa. It was. Here, in the water electrolysis gas generator, a water electrolysis gas is generated using a potassium hydroxide electrolyte, and the water electrolysis gas and LPG introduced into the mixing tank can be finely adjusted by a needle valve. It was configured as follows. Further, as an additional device for burning the water-electrolyzed gas mixed fuel gas, an LPG combustion burner for large-sized heaters used for commercial heating equipment and the like, model ELGU150 was used. The burner has an LPG rated consumption of about 2.4 m ³ per hour.

The experiment was conducted in the Kanto region (Saitama Prefecture) where the floor area of about 180m ² , galvanized steel sheet, and average ceiling height of about 5m were operated with the demonstration system configured as described above. Several experiments were performed at 20 ° C. for 1 hour. About 15 minutes after starting the demonstration device and supplying the water electrolysis gas and LP gas to the mixing tank, the operation of the water electrolysis gas generator is stopped and the introduction of the water electrolysis gas is stopped. However, no change was seen in the combustion state of the water electrolysis gas mixture fuel gas. After about 15 minutes, the operation of the water electrolysis gas generator was restarted, the introduction of water electrolysis gas into the mixing tank was started (restarted), and the introduction of LP gas was also started (restart). In this experiment, such a stop and start (restart) operation was repeated intermittently.

Experiment 1: January 18, 2008, Weather: Cloudy, outside temperature 3.2 ° C, room temperature 2.5 ° C before start
Experiment 2: January 19, 2008, Weather: Sunny, outside temperature 0.5 ° C, room temperature before start -0.2 ° C
The apparatus was operated for 1 hour each at a heater ejection temperature of 45 ° C and a set room temperature of 20 ° C. In both experiments, it was confirmed that the measured value; the average consumption of LPG was 0.71 m ³ / h, and the temperature rose to 18.5 to 20 ° C.
The average LPG consumption 0.71 m ³ / h in this case is only about 40% of the LPG rated consumption of the combustion burner. In addition, the amount of gasoline charged in the mixing tank during the experiment was only slightly decreased as confirmed by a level gauge. In addition, since water electrolysis was carried out in connection with the experiment, it was confirmed that although several kWh of electric power and a slight amount of make-up water were required, the amount of fossil fuel consumption was very small.

  Further, the concentration of carbon dioxide (CO2) in the combustion exhaust gas of the fuel obtained by the present invention is 5.4%, which is extremely low compared to 10.7% for heavy fuel oil A and 11.63% for LPG. Was confirmed. The concentration of nitrogen oxide (NOX) in the combustion exhaust gas of the fuel obtained by the present invention was 39 ppm, which was confirmed to be extremely low as compared with 79 ppm of A heavy oil. The combustion temperature of the fuel obtained by the present invention was 1,010 ° C., which was confirmed to be higher than that of 740 ° C. of A heavy oil.

  The water electrolysis gas mixed fuel generating apparatus according to the present invention detects the displacement of the ascending / descending movable portion ascending or descending or the change in the internal pressure of the mixing tank, and supplies the water electrolysis gas and the gas fossil fuel into the mixing tank. Since it is controlled to stop, when the water electrolysis gas mixed fuel generated according to the present invention is burned by a heating burner that burns conventional LPG or the like, LPG for obtaining the same amount of heat as combustion of only LPG About 40% is sufficient, and since the supply of water electrolysis gas is stopped under certain conditions, the power consumption for operating the water electrolysis gas generator is also reduced.

  The water electrolyzed gas mixed fuel produced by the water electrolyzed gas mixed fuel producing apparatus according to the present invention can generate heat more strongly than the original combustion of the fossil fuel itself, and hardly generate impurities accompanying the combustion. Therefore, the combustion efficiency is also greatly improved, so that naturally the consumption of fossil fuel is reduced, and the carbon dioxide emission accompanying combustion is also greatly reduced. Such a hybrid composite gas is obtained by water electrolysis, and the amount of electric power for water electrolysis is the main cost except for the initial capital investment, so the increase is small.

  Moreover, not only a direct combustion device at a developed part such as a normal burner, but also an internal combustion engine and a jet engine that explosively burn liquid fuel or gaseous fuel in a sealed space, liquid, gaseous, solid fuel can be used. In other large boilers for power generation to be used, it is expected that a stronger output than before can be obtained by adding and supplying each fuel or injecting it into the combustion chamber. In other words, a more powerful thermal energy output can be obtained with a fuel cost that is significantly reduced as compared with the prior art, and a significant cost saving can be expected. Therefore, a large energy saving effect can be obtained, and the amount of carbon dioxide emission can be significantly reduced in a reflective manner, so that it can be expected to exert an extremely large effect as a countermeasure against global warming. Moreover, it leads to effective use of fossil fuels with limited reserves on a global scale, and it is possible to extend the use period of each resource.

It is the schematic sectional drawing (A) of the production | generation apparatus of the water electrolysis gas mixed fuel which concerns on this invention, and AA sectional drawing (B) of FIG. It is a block diagram which shows the production | generation apparatus and related peripheral apparatus of the water electrolysis gas mixed fuel which concern on this invention. It is a block diagram which shows the basic structural example of the generator of the water electrolysis gas used for the production | generation apparatus of the water electrolysis gas mixed fuel which concerns on this invention. It is a figure which shows the structural example of the electrolytic vessel of the water electrolysis gas generator shown in FIG. It is a figure which shows the structural example of the single-piece | unit disk which comprises the metal plate group used for the electrolytic cell of the water electrolysis gas generator shown in FIG. It is the photograph which image | photographed the arrangement | positioning state of the whole demonstration apparatus for confirming the performance of the water electrolysis gas mixed fuel obtained by this invention. It is the photograph which image | photographed the state of the flame which generate | occur | produces from the combustion burner in the verification apparatus for confirming the performance of the water electrolysis gas mixed fuel obtained by this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Water electrolysis gas mixed fuel production | generation apparatus 11 Mixing tank 12 Water electrolysis gas supply means 13 Fossil fuel supply means 14 Water electrolysis gas mixed fuel discharge means 15 Lifting movable part 16 Outer peripheral surface outer frame part 17 Upper surface outer frame part 20 Control means 30 Water Electrolytic gas generator (water electrolysis device)
31 Electrolyte inlet 32 Anode plate (anode)
33 Cathode plate (cathode)
34 Electrolyte swirl flow means (metal plate group)
34-1 to n Metal plate 35 Mixture outlet 36 Electrolyte replenishment port 37 Cylindrical insulator 38 Line filter 39 Electrolyte outlet 40 Gas fossil fuel supply device (gas cylinder)
41 Inlet 42 Electrolyte outlet 43 Cooling electrolyte inlet 44 Circulation pump 45 Gas outlet 47 Electrolyte passage opening (opening)
51, 52, 53 Partition plate 54 Hanging part 55, 56, 57 Connecting rod 58 Opening part 60 Fuel use device 102, 103 Check valve 300 Electrolyzer for water electrolysis gas generation (electrolyzer)
301 Water electrolysis gas-electrolyte separation tank (separation tank)
302 Electrolytic solution forced cooling means 303 Electrolyte circulation means C Center point L Liquid S Crevice

Claims (13)

A mixing tank that contains a liquid selected from organic compounds such as alkane-based, alcohol-based, and ether-based substances inside, and repeatedly performs mixing of the supplied bubbly water electrolysis gas and gas fossil fuel; and the mixing Water electrolysis gas supply means for supplying water electrolysis gas generated by water electrolysis using a basic electrolyte to the tank in the form of bubbles, and fossil fuel supply means for supplying gas fossil fuel in the form of bubbles to the mixing tank And water electrolysis gas mixed fuel discharge means for discharging the water electrolysis gas mixed fuel generated by repeatedly performing the mixing of the water electrolysis gas and the gas fossil fuel to the fuel use device. In the device
A partition plate in which a plurality of pores are formed so that bubbles of the water electrolysis gas and gas fossil fuel cannot easily pass therethrough, and the partition plate is immersed in the liquid contained in the mixing tank, and the outer periphery of the partition plate An elevating movable part configured in an elevating movable structure to which a plurality of partition plates installed in the horizontal direction are attached in a state where the surface is close to the inner wall of the mixing tank,
Control means for controlling stop or start of supply to the mixing tank of the water electrolysis gas and / or gas fossil fuel, supply amount, and predetermined component ratio;
An apparatus for producing a water-electrolyzed gas mixed fuel, comprising:   2. The water electrolysis according to claim 1, wherein the liquid of the organic compound such as the alkane-based, alcohol-based, or ether-based substance is any one selected from gasoline, ethanol, methyl alcohol, and dimethyl ether. Gas mixed fuel generator.   The fossil fuel is any one of fossil fuels selected from liquefied petroleum gas (LPG), liquefied natural gas (LNG), and coal dry distillation gas. Water electrolysis gas mixed fuel generator.   The water electrolyzed gas mixed fuel produced by the water electrolyzed gas mixed fuel producing device includes a gas that is vaporized from a liquid of an organic compound such as the alkane-based, alcohol-based, or ether-based material. The apparatus for producing a water-electrolyzed gas mixed fuel according to any one of 1 to 3.   The partition plate attached to the elevating movable part is formed in three stages, and the lowermost partition plate is made of stainless steel having a thickness of 0.5 to 2.5 mm and a pore diameter of 0.5 to 3.5 mm, 5. The water electrolysis gas mixed fuel production according to any one of claims 1 to 4, wherein the upper partition plate is a flat mesh structure having a pore diameter of 0.2 to 1.5 mm. apparatus.   The control means gathers a large number of bubbles of the water electrolysis gas and gas fossil fuel on the lower surface side of the partition plate and the movement to the upper layer is stagnated, or the bubbles pass through the pores and move to the upper layer. And detecting the displacement of the ascending / descending movable part to which the partition plate attached to the unit is attached is controlled to stop or start the supply of water electrolysis gas and gas fossil fuel into the mixing tank. The apparatus for producing a water electrolysis gas mixed fuel according to any one of claims 1 to 5.   6. The control device according to claim 1, wherein the control means detects a change in the internal pressure of the mixing tank and controls the stop or start of the supply of water electrolysis gas and gas fossil fuel into the mixing tank. An apparatus for producing a water-electrolyzed gas mixed fuel according to claim 1.   The control means detects that the internal pressure of the mixing tank has reached the same pressure as the pressure set as the supply stop condition for the fossil fuel mixing tank, and stops the supply of water electrolysis gas into the mixing tank. And detecting that the internal pressure of the mixing tank is lower than the set pressure and controlling the start of the supply of water electrolysis gas into the mixing tank. The production apparatus of the water electrolysis gas mixed fuel of description.   The electrolysis apparatus for generating water electrolysis gas supplied to the water electrolysis gas supply means has an electrolyte introduction port on the bottom side and an extraction port for taking out a mixture of the electrolyte and product gas on the top side. An anode plate disposed on the bottom side in the electrolytic cell; a cathode plate disposed on the top side in the electrolytic cell; and alkaline electrolysis in a direction from the anode plate toward the cathode plate. An electrolytic cell for water electrolysis gas generation having an electrolysis solution swirl flow means without electrical connection for allowing the liquid to flow while swirling, and a water electrolysis gas taken out from a take-out port at the upper end of the electrolytic cell; Water electrolysis gas-electrolyte separation tank for introducing a mixture of electrolytes, separating the gas components of water electrolysis gas and electrolytes, taking out the gas components outside, and leaving the electrolyte components remaining And forced cooling of the electrolyte remaining in the separation tank. 9. A water electrolysis gas generator comprising: an electrolytic solution forced cooling means for carrying out the process; and an electrolytic solution circulation means for circulating the electrolytic solution to the electrolytic cell side. The production apparatus of the water electrolysis gas mixed fuel of description.   The electrolyte swirl flow means disposed between the anode plate and the cathode plate in the electrolytic cell is a required number of metal plates which are perforated in a point-symmetric manner by deviating from the center to the outer peripheral side. It has a structure in which the electrolyte solution is allowed to flow with swirling flow by arranging thirty-six flow openings and sequentially disposing the flow openings by a predetermined angle. 10. The apparatus for producing a water-electrolyzed gas mixed fuel according to 9, Water electrolyte gas generated by water electrolysis using basic electrolyte and gas fossil fuel are introduced in the form of bubbles, and a liquid selected from organic compounds such as alkanes, alcohols, and ethers is contained inside. In the mixing tank, the mixing is repeatedly performed so that the introduced water electrolysis gas and the fossil fuel are uniformly mixed,
A partition plate in which a plurality of pores are formed so that bubbles of the water electrolysis gas and gas fossil fuel cannot easily pass therethrough, and the partition plate is immersed in the liquid contained in the mixing tank, and the outer periphery of the partition plate Equipped with an elevating movable part configured in an elevating movable structure to which a plurality of partition plates installed in the horizontal direction are attached in a state where the surface is close to the inner wall of the mixing tank,
The partition generated by a large number of bubbles of the water electrolysis gas and gas fossil fuel gathering on the lower surface side of the partition plate and the movement to the upper layer stagnate or the bubbles passing through the pores and moving to the upper layer Detecting the displacement of ascending or descending of the movable part where the plate is mounted, controlling the stop or start of the supply of water electrolysis gas and gas fossil fuel into the mixing tank, the supply amount, the predetermined component ratio,
A method for producing a water electrolysis gas mixed fuel, comprising producing a water electrolysis gas mixed fuel in which mixing of the water electrolysis gas and gaseous fossil fuel is repeatedly performed.   The control of stopping or starting the supply of the water electrolysis gas and the gas fossil fuel into the mixing tank is performed by detecting a change in the internal pressure of the mixing tank. Generation method.   The control of stopping the supply of water electrolysis gas into the mixing tank detects that the internal pressure of the mixing tank has reached the same internal pressure as the mixing tank set as the supply stop condition for the fossil fuel mixing tank. The water electrolysis according to claim 11, wherein the control for starting the supply of the water electrolysis gas into the mixing tank is performed by detecting that the internal pressure of the mixing tank has decreased below the set internal pressure. Generation method of gas mixed fuel.

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