WO2018105133A1 - Dispositif à cycle fermé d'hydrogène liquide - Google Patents

Dispositif à cycle fermé d'hydrogène liquide Download PDF

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Publication number
WO2018105133A1
WO2018105133A1 PCT/JP2017/004574 JP2017004574W WO2018105133A1 WO 2018105133 A1 WO2018105133 A1 WO 2018105133A1 JP 2017004574 W JP2017004574 W JP 2017004574W WO 2018105133 A1 WO2018105133 A1 WO 2018105133A1
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Prior art keywords
hydrogen gas
food
hydrogen
drying
closed cycle
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Application number
PCT/JP2017/004574
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English (en)
Japanese (ja)
Inventor
杉山　修
Original Assignee
杉山　修
水口 果南
水口 侑香
水口 小春
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Priority claimed from JP2016238102A external-priority patent/JP2018093740A/ja
Priority claimed from JP2016006115U external-priority patent/JP3209283U/ja
Priority claimed from JP2017000033U external-priority patent/JP3209521U/ja
Application filed by 杉山　修, 水口 果南, 水口 侑香, 水口 小春 filed Critical 杉山　修
Publication of WO2018105133A1 publication Critical patent/WO2018105133A1/fr

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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23B—PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B4/00—General methods for preserving meat, sausages, fish or fish products
    • A23B4/03—Drying; Subsequent reconstitution
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23B—PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00—Preservation or chemical ripening of fruit or vegetables
    • A23B7/02—Dehydrating; Subsequent reconstitution
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/40—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by drying or kilning; Subsequent reconstitution
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M15/00—Inhalators
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/08—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents with metals
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
    • F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
    • F02C1/10—Closed cycles
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
    • F02C6/20—Adaptations of gas-turbine plants for driving vehicles
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • the present invention relates to a hydrogen fluid closed cycle apparatus such as a food drying apparatus, an antioxidant action imparting apparatus, a drive / power generation apparatus, and a power engine using a hydrogen fluid, and a method using the apparatus.
  • Patent Documents 1 to 8 Food, food waste, and other foodstuffs must be dried for storage, to be tasty, to reduce volume, to have the desired shape, to concentrate nutrients, and to regenerate as other forms of foodstuffs, etc.
  • Patent Documents 1 to 4 describe a method of drying food with air.
  • Patent Document 1 describes a method of drying food waste such as food processing residues with hot air
  • Patent Document 2 discloses a method of drying with hot air while crushing food raw materials in a sealed container.
  • Patent Document 3 describes a method for drying food that causes dehumidified cold air to collide with food on a conveyor having a large number of ventilation holes.
  • Patent Document 4 describes the direction of drying air produced by a refrigerator. A cold air drying device that blows air in a changed manner is described.
  • Patent Documents 5 to 8 describe a method of drying a food material with a gas other than air.
  • Patent Document 5 describes an apparatus for processing foodstuffs, and a drying apparatus having a passage for guiding a gaseous medium such as superheated steam from a horizontal direction and a vertical direction of a spiral conveyor belt
  • Patent Document 6 describes a method of drying a food material with superheated steam at a low temperature (100 ° C. or less) under reduced pressure.
  • Patent Document 7 describes a method for producing edible particles by contacting a supercritical medium made of carbon dioxide or nitrous oxide
  • Patent Document 8 describes a method for drying food by circulating gas.
  • As the gas a method using a gas having an oxygen concentration of 10% or less and nitrogen having a purity of 90% or more is described.
  • Patent Document 9 describes a method of generating hydrogen gas from “water in which hydrogen is dissolved” and inhaling the hydrogen gas from the nose.
  • Patent Documents 10, 11, and 12 describe a method for inhaling hydrogen gas generated by electrolysis of water from the nose or mouth, and an inhalation mask.
  • Patent Document 13 describes a method and sheet for preventing or suppressing cancer by bringing a water retaining layer holding “water in which hydrogen is dissolved” into contact with the skin.
  • the apparatus used in the above technique does not have a hydrogen gas generator inside, but obtains hydrogen from water in which hydrogen is dissolved (so-called “hydrogen water”). It was a wasteful stage to produce hydrogen gas from it.
  • electricity is used for electrolysis of water, and the equipment used there consumes electricity, uses industrial energy such as a steam reforming method, and heats hydrogen gas. I don't think that I will show the effect.
  • Patent Documents 14, 15, and 16 describe a hydrogen gas generator that brings alkaline water into contact with aluminum, silicon, or the like.
  • Patent Document 17 describes a direct-cycle engine that uses liquid hydrogen and liquid oxygen and uses volume expansion due to combustion.
  • Patent Document 18 describes a hydrogen engine characterized by a throttle using hydrogen gas as a fuel. However, all of these are those that burn hydrogen to gain energy.
  • Patent Document 19 describes an electric vehicle that uses hydrogen obtained by electrolyzing water as fuel for a fuel cell.
  • Patent Document 20 describes hydrogen obtained by catalytic reaction of methanol as fuel for a fuel cell. Is used as a power device. However, they all use hydrogen as fuel for the fuel cell to obtain electric power and consume hydrogen gas.
  • hydrogen gas has a low critical point and high thermal conductivity, and it is safe if oxygen is not present, there are technologies to obtain energy by burning and fuel cell fuel technologies. There are few techniques for obtaining kinetic energy (propulsion, rotational drive, etc.) or electrical energy (power generation by rotating a rotor blade with a fluid that does not depend on combustion) by using it as a fluid.
  • the present invention has been made in view of the above-described background art, and its problem is to provide a novel apparatus using a specific gas.
  • a novel food drying method a food drying apparatus, Providing a novel dry food production method; Providing a novel antioxidant device and antioxidant method; “Non-atmospheric energy closed cycle” that does not use the atmosphere and does not emit exhaust gas
  • the present inventor has used the above-mentioned problems by using hydrogen gas having features such as a low critical point, high thermal conductivity, and safety without oxygen. It was found that can be solved. Specifically, the present inventors have found an excellent effect that drying can be efficiently performed by using hydrogen gas as a medium used for drying food materials. In addition, the body can be effectively protected by using a combination of a hydrogen gas generator that generates only hydrogen gas through a chemical reaction and a member that allows the human to ingest the heated hydrogen from the temperature rising device. I found out that I can.
  • the present invention provides a hydrogen fluid closed cycle device characterized by comprising at least the following (1), (2) and (R).
  • (1) Hydrogen gas generator for generating hydrogen gas (2)
  • Hydrogen gas heating device and hydrogen gas utilization device that uses hydrogen gas from the temporary storage tank
  • the present invention includes the following aspect 1, aspect 2 or aspect 3 as a preferable aspect.
  • aspect 1 of the present invention is a food drying apparatus comprising the above hydrogen fluid closed cycle apparatus
  • the present invention provides a food drying apparatus that is used in a food drying method for removing water contained in the food by bringing hydrogen gas into contact with and passing through the food.
  • the present invention is a food drying method using the above-described food drying apparatus, wherein hydrogen is brought into contact with and permeated through the food to remove moisture contained in the food. A method is provided.
  • drying using the above-described food drying apparatus or the above-described food drying method allows hydrogen gas to contact and permeate the food to remove moisture contained in the food.
  • the manufacturing method of a foodstuff is provided.
  • Aspect 2 of the present invention is an antioxidant effect imparting device comprising the above hydrogen fluid closed cycle device,
  • the present invention provides an antioxidant effect imparting device characterized by comprising at least the following (a), (b) and (R2).
  • (A) Hydrogen gas generator for generating hydrogen gas by chemical reaction (b) Hydrogen gas temperature rise control device (R2) for raising the temperature of the hydrogen gas generated by the above (a) hydrogen gas generator (R2)
  • R2 Hydrogen gas temperature rise control device
  • the hydrogen gas Hydrogen gas inhalation mask that allows a human to inhale, or a hydrogen gas discharge filling container that makes the hydrogen gas contact a human or a part of the human
  • the second aspect of the present invention is to use the above-mentioned antioxidant action imparting device and raise the hydrogen gas stepwise while controlling the temperature of the hydrogen gas to bring the hydrogen gas into contact with a human or a part of the human.
  • the present invention provides a method for imparting an anti-oxidant action.
  • Aspect 3 of the present invention is a hydrogen fluid closed cycle drive / power generation device comprising the above hydrogen fluid closed cycle device,
  • the present invention provides a supercritical hydrogen fluid closed cycle drive / power generation device characterized by comprising at least all of the following (R3) and (R4).
  • (R3) Drive unit including a turbine that rotates when hydrogen gas is injected from the temporary storage tank (R4)
  • Fluid generator that generates power by rotating the rotor blades when hydrogen gas is injected from the temporary storage tank
  • Aspect 3 of the present invention provides a power engine equipped with the above hydrogen fluid closed cycle drive / power generation apparatus.
  • Aspect 3 of the present invention provides a driving / power generation method using the above-described hydrogen fluid closed cycle driving / power generation apparatus.
  • the food drying apparatus which is one form of the hydrogen fluid closed cycle apparatus according to the present invention and the invention related to the apparatus will be abbreviated as “Aspect 1”, and similarly, the antioxidant action imparting apparatus which is another form and the invention related thereto. Is abbreviated as “Aspect 2”, and similarly, another embodiment of the hydrogen fluid closed cycle drive / power generation apparatus and the invention related thereto are abbreviated as “Aspect 3”.
  • hydrogen gas having characteristics such as a low critical point and extremely high thermal conductivity; safe without oxygen; has an antioxidant effect; It is possible to provide an apparatus and a method that are easy, physically and chemically safe, have no toxicity, and are safe for living organisms. Further, it is an “closed cycle of energy” that does not burn and does not use the atmosphere, and can provide an apparatus that does not emit exhaust gas, pollutes the atmosphere, does not load the environment, and has low risk.
  • the effects of the aspect 1 of the present invention are as follows. Even if the food is not heated to a high temperature, it can be dried in a very short time.
  • the thermal conductivity of hydrogen gas is much higher than that of air, nitrogen gas, water vapor, methane gas, fluorine gas, or the like.
  • the thermal conductivity of hydrogen gas is higher than that of helium gas, which is known for its extremely high thermal conductivity.
  • hydrogen gas since hydrogen gas has a low critical point and high thermal conductivity, heat is easily transferred to the food, high-pressure fluid is easily generated, and the food can be dried in a short time.
  • hydrogen gas has high permeability and permeability to objects. For this reason, it penetrates and permeates the inside of an object (foodstuff) with high gas barrier properties and quickly dries the foodstuff. Therefore, for example, potatoes such as potatoes and sweet potatoes (skins); fruits such as apples, strawberries and oranges (skins); mushrooms such as jellyfishes; marine products such as fish, abalone and sea cucumbers; etc. It is also suitable for drying, roasting in an intermediate temperature range, non-flying heating and the like.
  • the nutrient value can be concentrated and dried while maintaining the shape of the food, increasing the commercial value.
  • the food drying method of aspect 1 of the present invention is applicable to (part of) eatable organisms themselves, non-standard vegetables, fruits and seafood, as well as secondary products generated during food processing. It can also be applied to food waste. Therefore, there is no waste of ingredients, and it is possible to provide ingredients with higher nutritional value.
  • the effect of the aspect 2 of this invention is the following.
  • the apparatus can be configured as a simple device, and the human body can be suitably protected on a daily basis. Specifically, without burdening the body against active substances, oxygen radicals, hydroxy (anion) radicals and other cells (species) that easily oxidize cells, intracellular tissues (organelles), and body substances It is possible to counter effectively.
  • the hydrogen fluid closed cycle drive / power generation device can be said to be a non-atmospheric hydrogen supercritical fluid closed cycle drive / power generation device, and basically does not require oxygen or air, and the drive / power generation energy is reduced to a low temperature. Created at (around 50-400 ° C). Since it does not depend on the atmosphere, it can be applied to non-atmosphere-dependent propulsion (AIP) submarines.
  • AIP non-atmosphere-dependent propulsion
  • the hydrogen used has a critical point of ⁇ 240 ° C. and 1.3 MPa, the highest thermal conductivity in the gas, and 0.1919 W / (m ⁇ K) under the condition of 50 ° C.
  • the air is 0.0272 W / (m ⁇ K) under the condition of 40 ° C. Compared to air, it has a thermal conductivity about 7 times that of a supercritical fluid even at low temperatures.
  • the hydrogen becomes supercritical in about 1 to 2 minutes.
  • the pressure is from 80 to 350 atm
  • the temperature is from 50 ° C to 400 ° C
  • the power generation capacity can be designed freely by setting the temperature and temporary storage time.
  • Temperature and pressure are in a proportional relationship, and the supercritical discharge state can be controlled by easily adjusting the temperature and pressure with a pressure control valve. If the impeller is directly rotated at a high speed as a supercritical fluid and the fluid power generator is directly rotated via the drive shaft, highly efficient electric power can be obtained.
  • a closed cycle operation can be performed by injecting and circulating a high-density active hydrogen gas fluid compressed and pressurized with power. Therefore, sunlight (electromagnetic waves), geothermal heat, other heat sources, “thermal expansion / waste heat by compressors, blanker pumps, etc.” can be used (recovered), and the hydrogen gas fluid can be driven at high pressure even at low temperatures. It is also possible to perform efficient rotation, drive and power generation.
  • an existing reciprocating engine diesel engine / rotary engine
  • a compression scroll engine or a single-shaft turbine
  • a single-shaft turbine is suitable because it can be operated in a closed cycle by thermal expansion.
  • an ignition spark plug, fuel, and air as in the existing engine are not required.
  • the hydrogen fluid closed cycle drive / power generation apparatus of the present invention uses a system that can be used as a power engine to achieve both driving and power generation.
  • FIG. 12 shows an example applied to a single-shaft turbine drive, but a supercritical pressure drive can supply a propulsive force and electric power, and a simultaneous output of at least 3 MW or more is possible.
  • FIG. 13 shows an example applied to a single-shaft turbine drive, but a supercritical pressure drive can supply a propulsive force and electric power, and a simultaneous output of at least 3 MW or more is possible.
  • the supercritical hydrogen fluid closed cycle drive / power generation device is effective in the maintenance of limited resources because no exhaust gas is produced and no fuel is consumed in gasoline. When applied to an automobile, it becomes a private power generation vehicle, and there is no exhaust emission of NOX during traveling.
  • the vehicle body can be lightened, and rare metals that are catalysts for fuel cells and the like are unnecessary. Moreover, the manufacturing cost is low, and it can be realized only by a combination of existing technologies. Since hydrogen gas is generated each time and is a continuous compression, heating system, or temporary storage system, a hydrogen compression storage tank is unnecessary. Hydrogen having a critical point of ⁇ 240 ° C. is less affected by the temperature, and if heated even below freezing, the hydrogen expands and becomes high pressure and becomes supercritical, so there is no decrease in output. It is a closed cycle system that does not consume fuel, and is highly energy efficient.
  • the hydrogen fluid closed cycle drive / power generation device of aspect 3 of the present invention is safe.
  • hydrogen gas has an ignition point of 570 ° C. in air and 450 ° C. in oxygen, and both are temperatures when oxygen is present.
  • hydrogen gas or “inactive with hydrogen” The “gas mixture” does not cause combustion or explosion. Only a hydrogen gas generator (alkaline ion water) is loaded, and even if there is a traffic accident, it does not explode because there is no high-pressure tank. There is no explosive fire because no fuel is loaded.
  • the hydrogen fluid closed cycle drive / power generation apparatus of aspect 3 of the present invention is optimal not only for the above-mentioned drive / power generation for consumer use, but also for the engine drive / power generation of ships and vehicles (see FIG. 13).
  • non-atmospheric propulsion for example, in the case of a submarine, an internal combustion diesel engine is usually used, and electric drive propulsion that floats, generates electric power, stores electricity, and dives.
  • the alkaline ion battery cannot store a large amount of electric power, and therefore cannot perform long-term stealth diving. Therefore, AIP (non-atmosphere-dependent propulsion) assists with a Stirling engine or the like, but the power generation capacity is as low as about 75 kW.
  • the closed cycle steam turbine engine used in the submarine burns a mixed gas of “oxygen obtained by vaporizing liquid oxygen as a supply source” and ethanol, and uses the combustion gas obtained at about 700 ° C.
  • a steam generator operates a steam turbine at 500 ° C. to generate electricity. There you need fuel.
  • the hydrogen fluid closed cycle drive / power generation device is a non-atmospheric supercritical closed cycle drive / power generation device (system). That is, it is a system that does not burn fuel, and the use of air in the ship is zero, which is extremely preferable for the ship environment. Since air and oxygen are not used and there is no exhaust gas, a large amount of power can be supplied from time to time within the ship, making it possible to covert underwater as long as a nuclear submarine. Submarine snorkeling is not required, and hydrogen gas production for leak replenishment can also be created in the ship (seawater fuel (hydrogen)) from drawn-in seawater.
  • system non-atmospheric supercritical closed cycle drive / power generation device
  • the hydrogen gas used as the heat medium is continuously generated by the method described later. Therefore, when a metal such as aluminum is separated from the alkaline water, the generation of the hydrogen gas stops immediately in only about 1 to 3 seconds. Therefore, there is no need for an adiabatic high-pressure tank such as liquefied hydrogen or a heavy hydrogen storage alloy, liquefied oxygen is unnecessary, and there is no explosion and it is extremely safe.
  • the supercritical hydrogen fluid having a high pressure is sequentially supplied from a plurality of temporary storage tanks, the rotating blades are rotated at a high speed, the drive shaft is rotated, and the power is driven.
  • This is a closed cycle system in which the fluid power generator is operated from the rotation of the shaft. Since air is not required, the internal combustion engine is not required (non-atmospheric energy), and the most technical point of the present invention is that hydrogen can be used as a supercritical fluid medium without burning.
  • the hydrogen gas is warmed and can be used in, for example, 1 to 2 minutes in a state of being temporarily confined in a plurality of sealed spaces (sealed containers).
  • FIG. 1 It is a conceptual diagram which shows an example of the aspect 1 of this invention. It is a schematic whole view showing an example of composition of a foodstuffs drying device of mode 1 of the present invention, and is a schematic diagram showing an example which has a foodstuff drying container and a foodstuff shelf. It is the schematic which shows an example of the structure of "the long and spiral food drying container" of the food drying apparatus of aspect 1 of this invention. It is a figure which shows the example of the photograph of the dry foodstuff from which the water
  • a photo of the ingredients are fish and the dried ingredients are fish meal
  • a photograph of the ingredients are fruits and the dried ingredients are dried fruits It is the schematic which shows an example of the antioxidant action provision apparatus of aspect 2 of this invention.
  • A) Cross-sectional view of antioxidant device (b) Photograph showing usage It is the schematic which shows an example of the antioxidant action provision apparatus of aspect 2 of this invention.
  • the drive device in aspect 3 of this invention is a rotary engine
  • the schematic which shows an example of the aspect of this rotary engine When the drive device in aspect 3 of this invention is a single shaft turbine engine, it is the schematic which shows an example of the aspect of this single shaft turbine engine. It is the schematic which shows an example of the aspect of this motor vehicle, when the hydrogen fluid closed cycle drive and electric power generating apparatus of aspect 3 of this invention is utilized for a motor vehicle.
  • the present invention is a hydrogen fluid closed cycle device comprising at least the following (1), (2) and (R).
  • (1) Hydrogen gas generator for generating hydrogen gas (2)
  • Hydrogen gas heating device and hydrogen gas utilization device that uses hydrogen gas from the temporary storage tank
  • the foodstuff dry container is the aspect 1
  • the (R) hydrogen gas utilization device of the present invention is a hydrogen gas suction mask or a hydrogen gas discharge full container, which is aspect 2.
  • the aspect (3) is that the (R) hydrogen gas utilization device of the present invention is a drive device including a turbine and a fluid power generator that rotates to generate electric power.
  • FIGS. 1 to 4 An example of the aspect 1 is shown in FIGS. 1 to 4, and “the reference numerals used in FIGS. 1 to 4” and “the reference numerals in the description of the aspect 1 below” are applied only to the aspect 1. To do. That is, “the reference numerals in the description of the aspect 1 described below” correspond to “the reference numerals used in FIGS. 1 to 4”, and the same reference numerals are used for the other elements in the description of other aspects and other drawings. Have been.
  • Aspect 1 of the present invention is a food drying apparatus comprising the above hydrogen fluid closed cycle apparatus, A food drying apparatus characterized by being used in a food drying method for removing water contained in the food by bringing hydrogen gas into contact with and passing through the food. Further, the present invention is a food drying method characterized by removing hydrogen contained in the food by contacting / permeating the gas with the hydrogen gas.
  • contact / transmission means “contact and / or transmission”. In the case of thick foods and the like, the case where it does not penetrate is also included.
  • the hydrogen gas to be used is not particularly limited, and may be generated by a chemical reaction or obtained by electrolysis of water or the like in a hydrogen gas generator attached to a food drying apparatus. It is preferable to use the hydrogen gas obtained by the above. Further, the reflux hydrogen gas from which the water vapor has been removed from the “hydrogen gas containing water vapor” once used as a drying medium may be heated and circulated again (closed cycle).
  • the temperature of the hydrogen gas immediately before contacting / permeating the food and the temperature of the hydrogen gas when contacting / permeating the food are not particularly limited, but are preferably 0 ° C. or higher and 100 ° C. or lower, more preferably 10 ° C. It is 60 ° C. or lower, particularly preferably 20 ° C. or higher and 40 ° C. or lower. Further, the temperature of the food during drying is not particularly limited, but it is preferable to dry the food so as to be in the above temperature range.
  • the temperature is equal to or higher than the above lower limit, it is not necessary to cool the hydrogen gas and a cooler is unnecessary, so that the water in the food does not freeze and it is difficult to remove the water.
  • the partial pressure (relative humidity) of water vapor contained in the hydrogen gas can be sufficiently reduced.
  • the hydrogen gas is preferably heated by the hydrogen gas heating device 28 before being introduced into the food drying container (see FIGS. 1 to 3). Heating facilitates drying, and heating in a sealed environment is particularly preferable because the pressure increases.
  • the temperature when the temperature is not more than the above upper limit, it becomes easy to dry without altering “various substances derived from living organisms” contained in food.
  • enzymes and vitamins should be 40 ° C. or lower, and preferably 38 ° C. or lower, so that decomposition and inactivation can be suppressed and drying can be facilitated.
  • the starch should be kept at 55 ° C. or lower, preferably 50 ° C. or lower, so that it does not change to ⁇ starch in the presence of water remaining in the drying ingredients, and is dried as ⁇ starch. Becomes easier.
  • the hydrogen gas to be introduced can be higher than the temperature while keeping the temperature of the food in the above range.
  • the pressure of hydrogen gas immediately before contacting / permeating the food material and the pressure of hydrogen gas contacting / permeating the food material are not particularly limited, but the hydrogen gas pressure is sealed before being introduced into the food drying container. It is also achieved by heating in the state. If the temperature of the hydrogen gas is raised, the pressure will increase, and the flow rate of hydrogen with an increased temperature will inevitably become faster, thus promoting drying. Moreover, hydrogen gas circulates and refluxes quickly.
  • the hydrogen gas may be introduced into the food material drying container through the inside of the hydrogen gas introduction pipe, or may be injected from the hydrogen gas introduction nozzle into the food material drying container.
  • the food drying apparatus 10 used in the food drying method of the present invention includes at least a hydrogen gas generator 20 that generates hydrogen gas, a food drying container 30 that stores the food F and allows hydrogen gas to pass, and a food drying container 30. It is preferable to include a dehumidifying device 40 that removes the water vapor from the “hydrogen gas containing water vapor” that has passed through the inside of the water.
  • FIG.1 and FIG.2 shows an example of a structure of the foodstuff drying apparatus 10 used for this invention.
  • Hydrogen gas generation (device)
  • the hydrogen gas used for drying may be separately brought into a cylinder or the like at a location away from the food drying apparatus 10, but in the hydrogen gas generator 20 associated with the food drying apparatus 10 of the present invention, a chemical reaction ( Or the amount of hydrogen required for drying is sufficient; there is no cost for cylinder charges, electricity charges, etc .; residual water exhausted by hydrogen gas is obtained as a useful byproduct; From the point of view, it is preferable.
  • the generation of hydrogen in the hydrogen gas generator 20 is preferably performed by bringing the alkaline water 22 into contact with the metal 21. That is, the hydrogen gas generator 20 in the present invention is preferably one that generates hydrogen gas by bringing the alkaline water 22 into contact with a metal.
  • the metal element is preferably a metal such as aluminum (Al), zinc (Zn), titanium (Ti), tin (Sn), etc., from the viewpoints of safety, cost (inexpensive), and useful products.
  • Aluminum is particularly preferred. Particularly in the case of aluminum, the reaction product is particularly preferable because it can be used as a purification material after filtration.
  • the metal 21 is preferably a metal 21 having a high ionization tendency.
  • the pH of the alkaline water is not particularly limited, but is preferably 12 or more, more preferably 13 or more, and particularly preferably 13.5 or more.
  • aluminum hydroxide (Al (OH) 3 ) produced on the surface of the aluminum is insoluble in water, so that the reaction is less likely to occur inside the metal.
  • Al (OH) 3 aluminum hydroxide
  • (strong) alkaline water having the above pH aluminum hydroxide is converted to aluminate ions and dissolved in water, the hydroxide film on the metal surface is dissolved, and the chemical reaction of the hydrogen gas activity is caused by the metal 21 Progress to the inside.
  • the produced aluminate (salt) should preferably be filtered off periodically.
  • a method of not precipitating aluminate (salt) by a simple technical operation has already been established, so that aluminate (salt) is not precipitated. You can also.
  • a stoichiometric amount of hydrogen gas of at least 1130 L or more can be obtained at high speed from 1 L of alkaline water in a standard state, so that the amount of hydrogen gas introduced into the food drying container 30 is sufficient.
  • the water after the reaction hydrogen generation is also clean transparent water.
  • the alkaline water 22 is obtained from natural products 27 such as natural stones (limestone, etc.), shells, meteorites, and the like because it is environmentally friendly.
  • FIG. 3 shows an apparatus for obtaining hydrogen from the alkaline water 22 by adding water to the natural product 27. Further, after the alkaline water is brought into contact with a metal 21 such as aluminum (Al) to generate hydrogen gas, it is not necessary to filter it by the above-mentioned technical operation. It is possible and environmentally friendly. Even when aluminate (salt) is precipitated by the reaction, the “filtered water obtained by filtering it” approaches neutrality.
  • the hydrogen gas to be introduced into the food drying container 30 passes through the inside of the food drying container 30 having the generated hydrogen gas generated by the hydrogen gas generator 20 and / or the food F, and “water vapor in the food
  • the reflux hydrogen gas obtained by removing the water vapor from the “hydrogen gas containing” can be used. It is preferable to supplement the recirculated hydrogen gas in a shortage due to leakage with the generated hydrogen gas.
  • the critical temperature of hydrogen is 33K ( ⁇ 240 ° C.), so it becomes supercritical by definition.
  • FIGS. 2 and 3 are schematic views of the hydrogen gas generator 20.
  • the metal 21 is moored and charged into the hydrogen gas generator 20 having the alkaline water 22 in the alkaline water tank 23, hydrogen gas is generated.
  • the generated hydrogen gas generated by the hydrogen gas generator 20 is introduced into the food drying container 30 through the hydrogen gas heating device 28, the temporary storage tank 26, and, if necessary, the dehumidifying filter 41.
  • the hydrogen gas is heated and pressurized by the hydrogen gas generator 20, the hydrogen gas heating device 28 and the temporary storage tank 26 while being introduced into the food drying container 30 (before).
  • the food drying apparatus 10 of the present invention has good drying efficiency because the hydrogen gas before being introduced into the food drying container 30 is heated and pressurized in the hydrogen gas heating device 28 and the temporary storage tank 26. It is essential from the point that the pressure can be raised.
  • the introduction of the hydrogen gas into the food material drying container 30 may be injected using a nozzle, or may be introduced or injected from below, but is more preferably introduced or injected from below.
  • the remaining water 24 can be orally used and can be effectively used for other purposes such as aquaculture water.
  • FIG. 2 shows an example of the food drying container 30.
  • the food drying container 30 in FIG. 2 has a “food material shelf 31 that is net-like and holds the food material from below” inside, and allows hydrogen gas to pass through the food material shelf 31, so that the food material F on the food material shelf 31 passes through the food material F on the food material shelf 31.
  • water contained in the food material F is removed by contacting and permeating hydrogen gas.
  • the food drying container 30 provided with the food shelf 31 is used for a relatively large dry food material as shown in FIG.
  • the food shelf 31 has a net-like shape so that the food F placed thereon does not fall down and allows hydrogen gas to pass from the bottom to the top.
  • the mesh size is not particularly limited as long as the above conditions are satisfied, but is preferably 0.1 mm or more and 100 mm or less, more preferably 0.5 mm or more and 50 mm or less, and particularly preferably 1 mm or more and 20 mm or less.
  • the “net-like” is also preferably “porous mesh-like”.
  • the form which put the basket on this net-like foodstuff shelf 31 may be sufficient. However, if the obtained dried food is in the form of powder as shown in FIG. 4B (for example, if it is expected to become powder), the mesh is further refined or the basket is placed on the food shelf 31. It is also preferable to place it.
  • the material of the net-like food shelf 31 is not particularly limited, and may be a net, a woven fabric, a perforated plate, or the like.
  • the material shelf 31 is not limited to any particular material, but may be any of metals, polymers such as synthetic resins, natural products such as wood, and the like. This is particularly preferable because it does not easily occur and does not cause a problem of metal embrittlement.
  • the number of the food shelves 31 in one food drying container 30 is not particularly limited, but is preferably 1 or more and 20 or less, more preferably 2 or more and 15 or less, and 3 or more and 10 or less. Particularly preferred.
  • a plurality of food drying containers 30 may be connected in parallel or in series (not shown). The connection may be vertical or horizontal, but it is preferable to arrange them horizontally because they are easy to work.
  • the food material F is appropriately cut as necessary, and is loaded into the food material drying container 30 from the food material charging hopper 37.
  • the generated hydrogen gas generated from the hydrogen gas generator 20 is heated to an appropriate temperature, and then introduced into the food drying container 30 using the hydrogen gas introduction pipe 32.
  • the injection position of the generated hydrogen gas to the food material drying container 30 may be anywhere, but as shown in FIG. 2, holes are made in the hydrogen gas introduction pipes 32 to hit the food material F, or particularly from below. It is particularly preferable from the viewpoint of drying efficiency.
  • the gas composed of “water vapor and hydrogen gas” from which moisture has been removed from the food material F is taken out from the “primary outlet 36 for water vapor and reflux hydrogen gas”, dehumidified in the pipe, and refluxed hydrogen gas transfer pipe 35 by the reflux hydrogen gas transfer pump 35. 33, and is introduced or injected into the food drying container 30 from the reflux hydrogen gas introduction nozzle 34 (FIG. 2).
  • the position where the reflux hydrogen gas is injected into the food drying container 30 may be from any location, and in the same manner as in the case of the generated hydrogen gas, holes may be made in places in the introduction pipe and applied to the food F from the side (not shown). 2), as shown in FIG. 2, it may be injected from below toward the food F by the reflux hydrogen gas introduction nozzle 34 from below.
  • the food drying container 30 has an elongated spiral shape, and the food F is placed on a hydrogen gas fluid to pass through the inside thereof, so that the moisture contained in the food F is contained. Those which are designed to be removed are also preferred.
  • the food drying container 30 that is elongated and spiral is preferably used in a form in which the dry food becomes powdery.
  • the food F is appropriately cut as necessary, and is loaded into the food drying container 30 from the food charging hopper 37.
  • the generated hydrogen gas generated from the hydrogen gas generator 20 is introduced into the food material drying container 30 from the vicinity of the starting point of the spiral food material drying container 30 using the hydrogen gas introduction pipe 32.
  • a gas composed of “water vapor and hydrogen gas” from which moisture has been removed from the food material F is taken out from the “primary outlet 36 of water vapor and reflux hydrogen gas” existing near the end point of the spiral food drying container 30, and is then refluxed hydrogen.
  • the gas is transferred through the reflux hydrogen gas transfer pipe 33 by the gas transfer pump 35 and introduced into the food drying container 30 from the vicinity of the starting point of the spiral food drying container 30 (FIG. 3).
  • reflux hydrogen gas transfer pipe 33 In the middle of the reflux hydrogen gas transfer pipe 33, it is preferable to provide a dehumidifier 40, where water vapor is removed, and the obtained dry hydrogen gas is introduced again into the food drying container 30 as reflux hydrogen gas.
  • Protrusions, baffles (buffers), etc. are provided on the inner wall of the elongated and spiral food drying container 30 to create a turbulent flow of hydrogen gas and move the food F in a zigzag manner.
  • water drainage pipes 42 (drain) (not shown) for collecting and extracting water droplets condensed on the inner wall of the food drying container 30 may be provided at places on the lower surface of the spiral food drying container 30. preferable.
  • Dehumidification (Device) The “gas consisting of water vapor and hydrogen gas” taken out from the “primary outlet 36 of water vapor and refluxing hydrogen gas” removes the water vapor by passing through the dehumidifying device 40, and the resulting dry hydrogen gas is refluxed. It is preferable to introduce or inject into the food drying container 30 as hydrogen gas.
  • the configuration of the dehumidifying device 40 is not particularly limited, it is preferable that the dehumidifying device 40 has a tank shape as shown in FIG. 2, and water droplets condensed in the tank are collected and extracted from the water drain pipe 42 (drain). Furthermore, it is preferable to provide a drain trap so that moisture is not entrained in the refluxing hydrogen gas.
  • the dehumidifying filter 41 is not particularly limited, and a known filter is used.
  • the dehumidifying device 40 is preferably a pipe having a built-in dehumidifying filter 41 because the dehumidifying effect is high.
  • the ingredients F may be pre-dried before being dried using the ingredients drying apparatus 10 of the present invention (before using the ingredients drying method of the present invention). It is also preferable to use the food F which has been pre-dried and which has been transported and stored.
  • the preliminary drying may be performed by a normal food drying method or the food drying method of the present invention. If the water content is 50% by mass or less by preliminary drying, practical storage is possible.
  • This invention is also a manufacturing method of the dried foodstuff characterized by using said foodstuff drying method. Moreover, it is also a manufacturing method of the dry foodstuff characterized by removing the water
  • the dried food obtained using the food drying method and the food drying apparatus 10 of the present invention include fish powder, meat powder, starch powder, dried fruit, and vegetable powder.
  • the obtained dried foods are supplements, dry powders, nutritional foods and health foods such as tablets; medical drugs such as powders (tablets); general foods such as sprinkles, dried fish and preserved foods; spices; It is useful as tea such as green tea and black tea; flour such as starch, rice flour, buckwheat flour and bread crumbs;
  • increasing the temperature is useful for roasting, non-fry cooking, and the like. Since hydrogen gas is highly permeable to objects and has high thermal conductivity, the dried food has a large volume of sea cucumber, abalone, fish, etc. It is mentioned as a particularly preferable one that has been utilized.
  • the thermal conductivity of hydrogen gas at 1 atm 0 ° C. is 168 mW / (m ⁇ K), whereas the thermal conductivity of air is 24 mW / (m ⁇ K).
  • the thermal conductivity of hydrogen gas at 1 atm. 25 ° C. is 185 mW / (m ⁇ K), whereas the thermal conductivity of air is 26 mW / (m ⁇ K).
  • the thermal conductivity of hydrogen gas at 1 atmosphere and 50 ° C. is 192 mW / (m ⁇ K), whereas the thermal conductivity of air is 28 mW / (m ⁇ K).
  • the thermal conductivity of hydrogen gas at 1 atm is about 7 times at any temperature relative to the thermal conductivity of air at 1 atm.
  • hydrogen gas has higher thermal conductivity at any temperature.
  • helium gas is much more expensive than hydrogen gas.
  • Embodiment 1 of the present invention is shown in FIGS. 1 to 3, but Embodiment 1 of the present invention is not limited to the specific embodiments shown in these.
  • the description of FIG. 1 will be described below.
  • Alkaline water 1 is injected in an appropriate amount leaving a space in the hydrogen gas generator 2.
  • the injected alkaline water 1 reacts with the metal 15 to continuously generate hydrogen gas.
  • the generated hydrogen enters the spiral heating tube in the microwave heating apparatus through the introduction tube and is heated to an appropriate temperature suitable for the nuclear food material.
  • the water vapor 6 is also generated from the microwave excitation heating device, the water vapor is also heated from the outer peripheral portion of the storage tank 7.
  • Example 1 The food material F was dried using the food material drying apparatus 10 schematically shown in FIG.
  • hydrogen gas generation apparatus (apparatus) (see FIG. 3)
  • alkaline water 22 obtained by adding water to natural product 27 including natural stones and shells was used, and aluminum was used as metal 21.
  • the temperature was set to 35 ° C. and introduced into the food drying container 30.
  • Hydrogen gas was blown onto the food material F placed on the food material shelf 31 made of polypropylene having an opening of 1 cm ⁇ 1 cm provided in the food material drying container 30.
  • the food drying container 30 was formed by connecting five food storage shelves 31 in parallel to each other.
  • Ingredients F are all non-standard in size and shape, and are carrots, grated burdock, burdock, and potato cut in advance to about 3 cm x about 1 cm x about 1 cm. It was predried by the drying method. A total of 5 kg was placed on the above-described 15-stage (three-stage ⁇ 5) food shelves 31, and heated hydrogen gas was injected from below.
  • a food drying container 30 having a “primary outlet 36 for water vapor and reflux hydrogen gas” and a “reflux hydrogen gas introduction nozzle 34” as shown in FIG. 2 is used.
  • the reflux hydrogen gas once used for drying was also used.
  • the refluxed hydrogen gas was dehumidified by passing through a dehumidifying device 40 provided with a dehumidifying filter 41 therein, and was made 35 ° C. and jetted upward from the bottom of the food drying container 30.
  • the time required from the start of drying to the end of drying was 10 minutes.
  • vitamins and enzymes were not decomposed (denatured) or inactivated and remained as they were.
  • the starch remained as beta starch.
  • the obtained vegetable chip was useful as a preserved food and a nutritional food.
  • Example 2 The foodstuff F was dried using the foodstuff drying apparatus 10 schematically shown in FIG. 3, and the same procedure as in Example 1 was used except that the fish preliminarily dried by a normal drying method was used until the water content reached 15% by mass. And dried.
  • Ingredient F is put in from the charging hopper, and hydrogen gas at 35 ° C. obtained in the same manner as in Example 1 is introduced into an “elongated and spirally shaped ingredient drying container 30” having an elliptical protrusion inside. Circulated.
  • the time required from the start of drying to the end of drying was 10 minutes.
  • the obtained fish meal was not decomposed (denatured) or inactivated, and remained as it was, and was useful as a preserved food, nutritional food, cooking additive, sprinkles and the like.
  • Example 1 drying was performed in the same manner as in Example 1 except that air was used instead of hydrogen gas, but 1 hour which was about 7 times as long as Example 1 from the start of drying to the end of drying. It took 10 minutes.
  • FIG. 5 to FIG. 7 An example of Aspect 2 is shown in FIG. 5 to FIG. 7, but “the reference numerals used in FIG. 5 to FIG. 7” and “the reference numerals in the description of Aspect 2 below” are applied only to Aspect 2. To do. That is, “the reference numerals in the description of the aspect 2 described below” correspond to “the reference numerals used in FIGS. 5 to 7”, and the same reference numerals are used in other aspects and other drawings. There may be.
  • Aspect 2 of the present invention is an antioxidant effect imparting device comprising the above hydrogen fluid closed cycle device, An antioxidant action imparting device characterized by comprising at least the following (a), (b) and (R2).
  • (A) Hydrogen gas generator for generating hydrogen gas by chemical reaction (b) Hydrogen gas temperature rise control device (R2) for raising the temperature of the hydrogen gas generated by the above (a) hydrogen gas generator (R2)
  • R2 Hydrogen gas temperature rise control device
  • the hydrogen gas Hydrogen gas inhalation mask that allows a human to inhale, or a hydrogen gas discharge filling container that makes the hydrogen gas contact a human or a part of the human
  • the hydrogen gas generator 2 used in the embodiment 2 of the present invention generates hydrogen gas by a chemical reaction. That is, “(1) a hydrogen gas generator for generating hydrogen gas” of the present invention is “(a) a hydrogen gas generator for generating hydrogen gas by a chemical reaction”. By generating hydrogen gas through a chemical reaction in the device provided in the antioxidant device 1, no intermediate product such as hydrogen water is required, and the hydrogen gas generator 2 does not consume electricity. Compactness can be achieved.
  • the one that can generate hydrogen gas by bringing the alkaline water 11 into contact with the metal 12 is the hydrogen necessary for the antioxidant effect imparting device of the present invention.
  • the amount is sufficient; since hydrogen gas of at least 1130 L can be obtained from 1 L of alkaline water, it can be made more compact, and costs such as cylinder charges and electricity charges are not required; See FIGS.
  • alkaline water before hydrogen gas generation obtained from natural products such as natural stone (limestone, etc.), shells, and meteorites has a very high calcium ion concentration. Containing water is obtained as a by-product.
  • FIG. 5A shows an outline of the hydrogen gas generator 2.
  • the generation of hydrogen in the hydrogen gas generator 2 is preferably caused by bringing the alkaline water 11 into contact with the metal 12.
  • the metal 12 includes alloys, and includes those processed into metal-containing materials.
  • the metal element is preferably a metal such as aluminum (Al), zinc (Zn), titanium (Ti), tin (Sn), etc., from the viewpoints of safety, cost (inexpensive), and useful products.
  • Aluminum (Al) is particularly preferable.
  • the metal 12 is also preferably a metal having a high ionization tendency.
  • the pH of the alkaline water is not particularly limited, but is preferably 12 or more, more preferably 12.5 or more, and particularly preferably 13 or more.
  • a stoichiometric amount of hydrogen gas of at least 1130 L can be obtained from 1 L of alkaline water in a standard state.
  • the amount of hydrogen gas used in the apparatus of the invention is sufficient.
  • the alkaline water 11 is not particularly limited, but it is particularly preferable to obtain the alkaline water 11 from natural products such as natural stones (limestone, etc.), shells, meteorites and the like because they are environmentally friendly. Further, even after the alkaline water 11 is brought into contact with a metal 12 such as aluminum (Al) to generate hydrogen gas, it can be taken orally without filtration by a technical operation method in which no aluminate is deposited. From that point, it is also environmentally friendly.
  • a metal 12 such as aluminum (Al) to generate hydrogen gas
  • Hydrogen gas generated by the hydrogen gas generator 2 is sent to the hydrogen gas suction mask 17 or the hydrogen gas discharge full container 27 through the hydrogen gas introduction pipes 15 and 23. In the meantime, it is preferable to pass through a dehumidifying filter 18 (not shown in FIG. 6) as shown in FIG.
  • a hydrogen gas temperature rise control device 3 for raising the temperature of the hydrogen gas is provided on the way.
  • the pressure is increased and the hydrogen gas is discharged or injected into the hydrogen gas discharge container 27 by using a nozzle, and the following effects are also achieved.
  • it is essential to provide a hydrogen gas heating device and a temporary storage tank (not shown in FIGS. 6A and 6B and FIG. 7).
  • the hydrogen gas heating device and the temporary storage tank may be installed before or after the hydrogen gas temperature increase control device 3, and the temperature rising portion or the like may be installed in the hydrogen gas temperature increase control device 3. It may be combined with the control device 3.
  • the appropriate temperature of hydrogen gas makes you feel better, increases the temperature of the human body, part of the human body, or the whole body, improves the basal body temperature, and improves blood circulation (blood flow Immunity is increased, and leukocytes are also increased and activated. It may also increase metabolic capacity and promote insulin secretion.
  • blood flow Immunity is increased, and leukocytes are also increased and activated. It may also increase metabolic capacity and promote insulin secretion.
  • the cancer cells exceed about 42 ° C., the proliferation is suppressed and apoptosis (self-destruction) is promoted, and as a result, the cancer cells may be reduced.
  • the antioxidant effect imparting device 1 is such that the hydrogen gas temperature raising control device 3 can be raised stepwise while controlling the temperature of the hydrogen gas at least in the range from 15 ° C. to 45 ° C. It is preferable that it is what is.
  • the preferred rate of temperature rise is gradually from the body temperature (about 36 ° C), preferably gradually over 2 minutes to 5 minutes, and raised to a maximum of 45 ° C ⁇ 1 ° C. This is preferable because there is little shock to heat, and hydrogen gas penetrates from the skin tissue into the blood and deep parts of the body (for example, cell walls, cell membranes, cell nuclei, bone marrow, etc.).
  • the time taken from 36 ° C. to 45 ° C. varies depending on the individual, but is more preferably 5 minutes to 20 minutes, and particularly preferably 10 minutes to 15 minutes, but is not limited thereto. Thereafter, keeping for 20 minutes or more is preferable in order to obtain the effect of the present invention.
  • Hot hydrogen gas inhalation mask Based on FIG. 5, an antioxidant action imparting device 1 having a hydrogen gas inhalation mask 17 for allowing a human to inhale the generated hydrogen gas will be described.
  • the aspect 2 of the present invention is limited to the specific aspect of FIG. 5. Is not to be done.
  • FIG. 5 is connected to a bottle main body containing alkaline water 11 (alkaline ion warm water) and metal 12, a connecting bottle 14, and a hydrogen gas introduction pipe 15 through which hydrogen gas passes, so that a medical condition, etc.
  • a hydrogen gas suction mask 17 having an appropriate shape corresponding to the application is connected (FIG. 5A).
  • FIG. 5B shows a state in which a human is sucking hydrogen gas from the hydrogen gas suction mask 17.
  • the metal 12 may be moored to the lid 13 so that it can be taken in and out as the lid 13 is opened and closed (may be detachable).
  • the bottle body preferably contains a medicinal component, an aroma component, and the like together with the alkaline water 11. It is also preferable to provide a dehumidifying filter 18 between the hydrogen gas introduction pipe 15 and the hydrogen gas suction mask 17.
  • the hydrogen gas suction mask 17 When the hydrogen gas suction mask 17 is used, it may not be provided to make the apparatus compact, but it is also preferable to provide the hydrogen gas temperature rise control device 3 to raise the temperature of the hydrogen gas.
  • the blood circulation In the case of warmed hydrogen gas, the blood circulation is increased, so that a more preferable result can be obtained quickly and the effect of the above-mentioned “warmed hydrogen gas” can be obtained.
  • Air is also inhaled at the same time, but air is only carried from the alveoli into the body, but hydrogen also penetrates into the obstructed brain.
  • the antioxidant effect imparting device 1 in FIG. 6A includes a hydrogen gas discharge filling container 27 that is brought into contact with the “whole body or body below the human neck”, and the antioxidant effect in FIG. 6B.
  • the applying device 1 includes a hydrogen gas discharge filling container 27 that is brought into contact with “a part of a person”.
  • FIG. 6B shows an example of a breast, but “part of a human” is not limited, and examples thereof include a breast, a torso, a back, a chest, a waist, and a limb.
  • the “part of human” is preferably an affected area, and a lymph gland is also preferable.
  • the normal temperature hydrogen gas generated from the hydrogen gas generator 2 enters the hydrogen gas temperature rise control device 3 through the hydrogen gas introduction pipe 23.
  • the configuration of the hydrogen gas temperature increase control device 3 is not particularly limited, but hydrogen gas enters the “spiral tube tube immersed in the thermostatic bath” and gradually increases in temperature while being controlled within the above temperature range. It is preferable that it is such.
  • the hydrogen gas heated to an appropriate temperature is guided to the hydrogen gas discharge full container 27 at the upper part of the mat 24 and comes into contact with a human.
  • the hydrogen gas discharge filling container 27 for bringing the hydrogen gas into contact with the human is, for example, one that contacts (contacts) the hydrogen gas toward the human (the whole) from a porous film vent pipe. Is preferred.
  • the hydrogen gas filling the hydrogen gas discharge filling container 27 contacts the human body, a part of the hydrogen gas penetrates and penetrates deep into the body, and then, for example, is installed in the upper part or the like.
  • the hydrogen gas discharge port 25 passes through the hydrogen gas return pipe 26 and circulates to the hydrogen gas temperature raising control device 3.
  • a drain trap 28 containing a dehumidifying material 31 is preferably provided in the middle, preferably in a vertical part, and moisture in the hydrogen gas is preferably removed by the drain trap 28 (FIG. 6A). .
  • the hydrogen gas from which moisture has been removed again enters the hydrogen gas temperature increase control device 3 and is circulated after being heated.
  • a hydrogen gas inhalation mask 17 as shown in FIG. 5 (a) is used in combination with a hydrogen gas discharge / filling container 27 for "the whole human body or the body below the human neck” as shown in FIG. 6 (a). May be. Warm hydrogen gas aspirated (with air) from the oral cavity, nasal cavity, etc. through the hydrogen gas inhalation mask 17 is taken into the body and brain tissue.
  • the antioxidant effect imparting device 1 of FIG. 6B includes a hydrogen gas discharge filling container 27 that is brought into contact with a breast that is “a part of a human being”. 6A, the hydrogen gas that has passed through the hydrogen gas introduction pipe 23 from the hydrogen gas generator 2 is heated through the thermostatic bath, and passes through the hydrogen gas introduction pipe 23. The hydrogen gas discharge filling container 27 is discharged or filled therein. Hydrogen gas is radiated to the affected area under the control of the temperature range and the rate of temperature increase, and the temperature is gradually raised from about 36 ° C. and heated to a maximum of about 45 ° C. At this time, a flexible cloth may be applied between the body and the body.
  • the thermal conductivity of hydrogen gas is much higher than that of air, nitrogen gas, water vapor, methane gas, fluorine gas, or the like.
  • the thermal conductivity of hydrogen gas is higher than that of helium gas, which is known for its extremely high thermal conductivity.
  • hydrogen gas has high permeability and permeability to objects. Due to its high permeability, when it comes into contact with humans, it easily penetrates into the inside (for example, cells and organs).
  • a particularly preferred embodiment of the invention will be described as part of a human being, for example but not limited to the breast.
  • the hydrogen gas generated from the hydrogen gas generator 2 is subjected to precise temperature control in a thermostatic chamber in the heating tube of the hydrogen gas temperature rise control device 3, and is gradually heated from room temperature, and then the radiant cup ( Radiated from the hydrogen gas-filled container 27) to the affected area (breast), gradually heated from 36 ° C and heated to 45 ° C. Since the temperature rises gradually, there is no shock to the heat. Since hydrogen is light, the radiation cup (hydrogen gas discharge full container 27) needs to be directed from the bottom to the top. At this time, you may apply a flexible cloth between affected part positions. Hydrogen penetrates and permeates with heat from skin tissue to blood and deep cells and organs. In particular, cancer cells are vulnerable to heat and self-destruct at around 42 ° C.
  • FIG. 7 Using FIG. 7 as an example, a particularly preferred embodiment of Embodiment 2 of the present invention will be described.
  • the concave portion of the mat 24 formed with irregularities there are several rows of vent pipes 29 and dozens of vent holes 30, and the vent holes 30 are heated and heated to an appropriate temperature by the hydrogen gas temperature rise control device 3 such as a thermostatic bath. Hydrogen gas is injected and emitted into the body (FIGS. 7A and 7D).
  • the convex portion of the rug such as the mat 24 functions as a cushion for humans.
  • a cloth that absorbs sweat The cloth may be the clothes of the human body.
  • the upper portion of the mat 24 is covered with an aluminum laminated sheet to protect the hydrogen gas from leaking.
  • An example of a preferable material for the hydrogen gas container 27 and the mat 24 is shown in FIG.
  • the material is preferably a laminate of aluminum foil.
  • a hydrogen gas return pipe 26 that collects and recirculates the hydrogen gas that has contacted (penetrated) the body is connected to a substantially central portion of the sheet.
  • the hydrogen gas return pipe 26 is made of an aluminum foil laminated pipe material 32, and it is preferable that a dehumidifying material 31 for adsorbing moisture in hydrogen gas containing moisture evaporated and sweated by heat is inserted in the inner diameter of the pipe ( FIG. 7B).
  • a drain trap 28 for discharging these moisture is installed below the hydrogen gas return pipe 26.
  • An appropriate amount of hydrogen gas discharged from the hydrogen gas generator 2 through a valve is released from the vent hole 30 via a hydrogen gas heating device and a temporary storage tank. Specifically, it enters a heating tube set inside a thermostatic chamber which is the hydrogen gas temperature raising control device 3, is heated to an appropriate temperature and gradually heated, and the hot hydrogen gas is a number inside the mat 24. It is discharged from the lower side of the human body toward the human body through the vent holes 30 of the dozens of vent pipes 29 in a strip. Since hydrogen gas is light, it diffuses immediately to the upper side, so it is preferable to discharge from the lower side (FIG. 7A).
  • FIGS. 8 to 13 An example of the aspect 3 is shown in FIGS. 8 to 13, but “the reference numerals used in FIGS. 8 to 13” and “the reference numerals in the description of the aspect 3 below” are applied only to the aspect 3. To do. That is, “the reference numerals in the description of the aspect 3 described below” correspond to “the reference numerals used in FIGS. 8 to 13”, and the same reference numerals are used in other aspects and other drawings. There may be.
  • Aspect 3 of the present invention is a hydrogen fluid closed cycle drive / power generation device including the above hydrogen fluid closed cycle device, A hydrogen fluid closed cycle drive / power generation device comprising at least all of the following (R3) and (R4): (R3) Drive unit including a turbine that rotates when hydrogen gas is injected from the temporary storage tank (R4) Fluid generator that generates power by rotating the rotor blades when hydrogen gas is injected from the temporary storage tank
  • the present invention comprises (1) a hydrogen gas generator, (2) a hydrogen gas heating device and a plurality of temporary storage tanks, and (R) a hydrogen gas utilization device, and (R) a hydrogen gas utilization device.
  • the apparatus has the (R3) driving device and (R4) fluid power generator.
  • the hydrogen fluid closed cycle drive / power generation apparatus 01 of the present invention includes (1) a hydrogen gas generator 11.
  • Generation of hydrogen in the hydrogen gas generator 11 is not particularly limited, but is caused by bringing alkaline water into contact with a metal. That is, it is preferable that the hydrogen gas generator 11 in the present invention is configured to generate hydrogen gas by bringing alkaline water into contact with a metal.
  • the metal element is preferably a metal such as aluminum (Al), zinc (Zn), titanium (Ti), tin (Sn), etc., from the viewpoints of safety, cost (inexpensive), and useful products.
  • Aluminum is particularly preferred. Particularly in the case of aluminum, the reaction product is particularly preferable because it can be used as a purification material after filtration. Further, as the metal, a metal having a high ionization tendency is also preferable.
  • the pH of the alkaline water is not particularly limited, but is preferably 12 or more, more preferably 13 or more, and particularly preferably 13.5 or more.
  • a stoichiometric amount of hydrogen gas of at least 1130 L can be obtained from 1 L of alkaline water in a standard state, which is sufficient as the amount of hydrogen gas.
  • alumina does not precipitate due to the reaction between the metal and the alkaline ionized water, filtration is not necessary, and the residual water is very effective as a clear and useful oral water. This technical operation has already been found.
  • the alkaline water is not limited, it is particularly preferable to obtain it from natural products such as natural stones (limestone, etc.), shells, meteorites and the like because they are environmentally friendly.
  • natural products such as natural stones (limestone, etc.), shells, meteorites and the like because they are environmentally friendly.
  • ionized alkaline water is obtained.
  • the alkaline water is brought into contact with a metal such as aluminum (Al) to generate hydrogen gas.
  • the generated hydrogen gas generated by the hydrogen gas generator 11 can be used. It is preferable to supplement the recirculated hydrogen gas in a shortage due to leakage with the generated hydrogen gas.
  • the critical temperature of hydrogen is 33K (-240 ° C).
  • the hydrogen gas heating apparatus is used by heating the hydrogen gas in a sealed container (sealed container) such as the temporary storage tank 13 to preferably 400 ° C. or lower. . See FIGS.
  • residual water after hydrogen gas generation can be extracted and substances such as generated aluminate can be removed.
  • the filtered water of the residual water can be taken orally and can be used effectively for other purposes such as aquaculture water.
  • Aluminic acid (salt) can also be effectively used as a purifier.
  • the hydrogen gas generator 11 is created by creating water with a high hydrogen ion concentration by a special method from natural resources with excellent environmental characteristics.
  • the hydrogen gas generator 11 is submerged in water with an inexpensive catalyst moored in the high ion concentration water. Since hydrogen gas is continuously generated, pure metal gas is produced by adding the metal in a timely manner when necessary. Therefore, a pressure-resistant container is not necessary, and a simple alkali-resistant resin container (for example, polyethylene, polypropylene, etc.) is sufficient.
  • the water used as the source of hydrogen gas generation used in the present invention is preferably used for medical purposes or foods.
  • seawater or terrestrial water is used as the water to produce alkaline water. Ionic water may be used.
  • seawater there are many mineral components, and more hydrogen gas is produced (already tested).
  • Hydrogen gas may be hydrogen alone (pure), but other gases can be mixed and used as a mixed gas.
  • the mixed gas has an effect of preventing “hydrogen embrittlement inherent to hydrogen gas” to the furnace body and the like.
  • hydrogen gas and “another inert gas such as carbon dioxide, nitrogen, argon, helium” are particularly preferable.
  • nitrogen, carbon dioxide and the like are more preferable.
  • carbon dioxide (CO 2 ) critical point: 31.1 ° C., 7.4 MPa) having a good cost performance is particularly preferable.
  • a mixed gas in which 95 to 98 parts by volume of hydrogen gas and 2 to 5 parts by volume of carbon dioxide gas are mixed is preferable.
  • the mixing ratio for example, “95% by volume of hydrogen, 5% by volume of carbon dioxide (CO 2 )”, “98% by volume of hydrogen, 2% by volume of helium” and the like are particularly preferable.
  • Hydrogen gas is a supercritical fluid even at a low temperature (for example, around 100 ° C.), the entire apparatus is light, no weight design is required, and the cost is low.
  • the engine apparatus can be manufactured by a 3D printer.
  • the hydrogen fluid closed cycle drive / power generation device 01 includes (2) a hydrogen gas heating device 12 that temporarily raises the pressure of the hydrogen gas by raising the temperature of the hydrogen gas generated by the hydrogen gas generator 11, and a temporary A mechanical storage tank 13 is provided.
  • the hydrogen gas heating device 12 and the temporary storage tank 13 are configured so that the hydrogen gas in the sealed temporary storage tank 13 is 400 ° C. or less. It is preferable to heat and use.
  • the heated hydrogen gas sequentially enters the temporary storage tank 13 (preferably 2 to 4 units), and after the sealed state has passed for about 1 to 2 minutes, the hydrogen gas is increased in pressure even in a low temperature region (50 ° C.). At this time, it becomes a supercritical fluid, and its pressure becomes about 20 MPa or more. Although the pressure of the hydrogen is increased, the storage time in the temporary storage tank 13 is only a few minutes, and an advanced pressure-resistant tank is not required, and the discharge is sequentially performed after 1 to 2 minutes, which is safe.
  • This high-pressure supercritical hydrogen sequentially flows into the pipe through the pressure control valve and the injection device, and is heated and temporarily stored in the fluid power generator 14 without burning the hydrogen gas.
  • the rotating blades are rotated at high speed by the hydrogen gas fluid generated to generate power from the drive shaft. It is preferable to evacuate the piping of each piece of equipment and the inside of the power engine in advance and then inject after filling with a mixed gas such as heated hydrogen gas or “hydrogen gas and carbon dioxide”. This is a common matter of the apparatus of the present invention (applied to plants, automobiles, etc.).
  • Hydrogen gas pressurized by heating with the heated steam 16 or the like enters a compression device such as a compression scroll engine, a rotary engine, or a single-shaft turbine, which is a power engine, and is driven and compressed through an exhaust port. Circulate and reflux again. Thus, it is non-atmosphere and low temperature, and it is possible to create driving force and electric power in various environments such as outer space, deep underground space, and highland.
  • a compression device such as a compression scroll engine, a rotary engine, or a single-shaft turbine, which is a power engine, and is driven and compressed through an exhaust port. Circulate and reflux again.
  • it is non-atmosphere and low temperature, and it is possible to create driving force and electric power in various environments such as outer space, deep underground space, and highland.
  • Hydrogen gas exiting from the hydrogen gas generator 11 enters a spiral heating tube or the like from the introduction pipe, is heated by the hydrogen gas heating device 12, enters the temporary storage tank 13, and is pressurized.
  • the hydrogen gas heating device 12 is used by heating the hydrogen gas in the temporary storage tank 13 to 400 ° C. or less.
  • the pressurized hydrogen gas is injected toward the intake port of the fluid power generator 14 to drive the rotor blades.
  • the pressurized hydrogen gas from the exhaust port merges with the fluid ejected from the temporary residual heat storage tank on the lower side, and returns to the temporary storage tank 13 again while driving the next rotor blade via the aspirator. It is heated and circulated with heated steam 16 (for example, about 300 ° C.).
  • the hydrogen fluid closed cycle drive / power generation device 01 includes (3) a drive device including a turbine that rotates when hydrogen gas is injected.
  • the hydrogen fluid closed cycle drive / power generation device 01 of the present invention includes (4) a fluid power generator that generates power by rotating the rotor blades when hydrogen gas is injected.
  • An alternator linked to the operating shaft of the rotor blade of the fluid power generator 14 generates power in a closed cycle manner, and drives or partially charges the storage battery 19.
  • a catch pan 17 is set at the lowermost part, and is discharged and collected from the drain trap 17. Excess process steam may be refluxed. Since this device (system) is basic, it can be used for, for example, those described later, and can be widely applied to disasters, private power generation, cars, ships, trains, submarines, space navigation, and the like.
  • Microwave excited water plasma heating device 12 is heated using microwaves or the like as non-atmosphere.
  • the mode and characteristics of the microwave-excited underwater plasma heating device 12a, which is a particularly preferable mode of the hydrogen gas heating device 12, will be described below with reference to FIG.
  • the microwave is initially driven by electricity from the storage battery 19.
  • 1 The configuration is such that the rotor blades are rotated at high speed with supercritical hydrogen gas, the structure is simple without using an internal combustion engine or a compression device, and maintenance is easy and quiet.
  • 2 Hydrogen is not combusted, is used in a closed cycle, and is not fuel. A high-pressure tank is unnecessary and safe, and hydrogen gas is generated when a metal that chemically reacts when necessary and moored together with a weight, and generation stops when removed.
  • 3 The catalyst of underwater plasma is a permanent catalyst. 4: Exhaust gas is zero and power can be generated indoors. Further, air (oxygen) is not necessary and can be used in a non-atmospheric space.
  • I POWER inorganic heating board that generates heat by microwaves can also be used semi-permanently. 6: Since the power generation stops when the start of the microwave is stopped, it may be started when power is required. A microwave output of 100 to 200 W is sufficient.
  • FIG. 10 shows a compression scroll type engine drive / power generation device 02 as an application example of the hydrogen fluid closed cycle drive / power generation device 01 of the present invention.
  • the compression scroll type engine drive / power generation device 02 is a device that drives and / or generates power with the scroll type engine 32, and uses compression (expansion) scroll type engine drive / power generation, and is applied to private power generation, automobiles, and the like.
  • Hydrogen gas sequentially generated from the hydrogen gas generator 11 reaches a critical point at room temperature.
  • this hydrogen gas or hydrogen mixed gas When this hydrogen gas or hydrogen mixed gas is injected from the sealed temporary storage tank 13 and flows as the scroll engine 32 through the suction port 34 near the center of the fixed blade, it is compressed between the movable blades and is pressurized. And expand, and the rotation shaft at the center can be rotated and driven.
  • the expanded hydrogen gas moves to the exhaust port 35, returns to the original temperature, and returns to the circulation pipe 36 from the discharge port.
  • the hydrogen gas returns to the center of the scroll type engine 32 again, is compressed and pressurized, and repeatedly performs a closed cycle operation.
  • the pressure is preferably 8 MPa or more. It is a closed-cycle operation and basically does not require fuel. Drive and power generation are possible from this rotating shaft.
  • the speed can be controlled by adjusting the flow rate of hydrogen gas with an accelerator pedal, and the engine brake is applied when the accelerator is released. Since the power is generated by the compression scroll engine 32, it can be said to be a “self-generated power vehicle”. Hydrogen gas is generated by the above-described chemical reaction from the loaded water and is driven by a continuous compression process, so it is extremely safe without the need for loading compressed liquefied hydrogen gas.
  • FIG. 11 shows a rotary engine drive / power generation device 03 as an application example of the hydrogen fluid closed cycle drive / power generation device 01 of the present invention.
  • the normal temperature hydrogen gas reaching the critical point is sucked into the suction port 34, and the pressure is increased in the sealed temporary storage tank 13, and is injected into the rotary engine 41 from the pressure regulating valve.
  • the rotary engine 41 is driven in the step (3) in which the pressure is further increased and the pressure becomes higher and higher in (4), and the body is rotated by the body expansion pressure.
  • the compression ratio of a normal rotary engine is 7-8, and hydrogen gas is 10 atmospheres or more in a supercritical fluid state.
  • the hydrogen in the step (3) in which the expansion is completed decreases in temperature, exits from the exhaust port 35, circulates, returns to the intake port 34 from the circulation pipe 36, and repeatedly performs closed cycle driving and power generation.
  • This rotary type engine drive / power generation device uses an engine drive system that is completely different from the combustion of ordinary fossil fuels, and is the most suitable environmental technology for global warming countermeasures, air pollution countermeasures, and resource reduction. Even with a normal diesel engine or reciprocating engine, the present invention can be carried out with a slight improvement. However, since there is metal embrittlement inherent to hydrogen gas, it is preferable to use a mixed gas of 95% by volume of hydrogen gas and 5% by volume of carbon dioxide, or the equipment is manufactured by ceramic spraying.
  • FIG. 12 shows a (non-atmosphere) single-shaft closed cycle turbine 53 and a single-shaft turbine engine drive / power generation device 04 as an application example of the hydrogen fluid closed cycle drive / power generation device 01 of the present invention.
  • the sealed temporary storage tank 13 is filled with hydrogen gas (mixed gas) for preheating.
  • the hydrogen gas (mixed gas) heated by the hydrogen gas heating device 12 is temporarily stored to increase the pressure.
  • the microwave-excited underwater plasma heating device 12a is provided with a gas heating tube, and the sunlight / waste heat / steam heating device 12b is provided with a hydrogen gas heating two-layer tank.
  • Compressed return gas is injected to the main turbine side and driving force is improved.
  • the gas exhausted from the single-shaft (closed cycle) turbine 53 returns to the microwave-excited underwater plasma heating device 12a again through the heat exchanger 55, is again heated and stored, returns to the compressor in a high-pressure state, and is driven. It becomes a cycle to repeat.
  • the fluid generator 54 and the drive motor 56 (generator possible) interlocked with the single-shaft turbine shaft are driven.
  • the temperature is about 100 ° C. and the pressure is about 20 MPa to about 35 MPa.
  • closed cycle power generation can be performed even at low temperatures.
  • Various waste heat, natural energy such as sunlight and geothermal ocean temperature difference can be recovered.
  • the hydrogen fluid closed cycle drive / power generation device 01 of the present invention can be used (mounted) in a power engine such as an automobile or a ship.
  • FIG. 13 shows a case where the hydrogen fluid closed cycle drive / power generation apparatus 01 of the present invention is applied to an automobile (for example, a new hybrid car) 05 as an application example.
  • the new hybrid vehicle 05 using the hydrogen fluid closed cycle drive / power generation device 01 of the present invention achieves both a driving motor propulsion force and a power generation function.
  • 1 Driven by motor 65 only when starting.
  • the motor 65 is an AC synchronous motor and preferably has a three-phase AC.
  • 2 During low-speed traveling with closed-cycle main power, the closed-cycle engines 02 and 03 are divided into two systems by the power split mechanism 64. One drives the motor through a path for generating electricity by driving the generator, and the other directly rotates the wheels via the gear transmission 66.
  • 3 When accelerating, it accelerates with two powers. By adding “engine driving force and power from the storage battery 19” and “high-power motor driving force”, smooth power performance with good response is exhibited and acceleration performance is improved.
  • the wheels and drive shaft 67 act on the motor 65 to operate the high-output motor (power control unit 63) as a generator to convert the braking energy of the car into more power. It acts as a highly efficient regenerative brake, and the collected electric power charges the storage battery 19.
  • the power control unit (PU) 63 has a function of converting a direct current and an alternating current to adjust a power supply voltage, and preferably includes an inverter, a variable voltage system, and a DC / DC converter.
  • the power split mechanism 64 is preferably linked to the drive train and the generator by various gears in the planetary gear mechanism.
  • the regenerative brake refers to a motor that rotates when electricity is applied, but generates electric power as a generator when rotated by an external driving force.
  • the hydrogen gas in the present invention has characteristics such as a critical point at low temperature, extremely high thermal conductivity, safety without oxygen, and an antioxidant effect, and is easy to raise and pressurize. Because it is physically and chemically safe, non-toxic and safe for the living body, it is a closed cycle that does not use the atmosphere, exhaust gas is not emitted, the atmosphere is not polluted, and the environment is not burdened. It can be used in various fields.
  • the food drying method and the food drying apparatus using the hydrogen gas of aspect 1 of the present invention as a drying medium are particularly excellent in drying efficiency and the like, and the raw material is also targeted for non-standard products, waste products, etc. Ingredients that are difficult to handle, large ingredients, etc. are also targeted, and the resulting dried ingredients are used in various applications, so they are widely used in food processing industries, household food industries, agriculture, fisheries, waste disposal industries, etc. It is what is used.
  • the antioxidation-effect imparting device is an anti-oxidation effect imparting device that has a hydrogen gas inhaled by a human inhalation or is brought into contact with the whole human or “part of an affected area”. Since the disease can be cured or relaxed by oxidizing and preferably raising the immunity by raising the temperature, it is widely used in the field of health equipment, the medical field, and the like.
  • the hydrogen fluid closed cycle drive / power generation device is a closed cycle, does not put a load on the environment, and has low risk. It is widely used in all fields.
  • FIG. 1 Alkaline water 2: Hydrogen gas generator 3: Microwave excitation: Heating part 4: Hydrogen gas introduction heating tube 5: Water 6: Water vapor 7: Temporary storage tank 8: Preliminary drain 9: Heated hydrogen gas injection hole DESCRIPTION OF SYMBOLS 10: Drying furnace 11: Shelf sliding mesh drying net 12: Recirculating hydrogen gas 13: Drain trap 14: Drain water 15: Metal 16: Filtration device 17: Filtration water 18: Catalyst mooring lid 19: Microwave unit 20: Vertical Dehumidifying material 21 in piping: Piping 22: Process steam

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Abstract

L'invention concerne un dispositif à cycle fermé d'hydrogène liquide qui comprend (1) un générateur de gaz hydrogène qui génère de l'hydrogène gazeux, (2) un dispositif de chauffage de gaz hydrogène et un réservoir de stockage temporaire qui élèvent la pression du gaz hydrogène en élevant la température du gaz hydrogène émis par (1) le générateur de gaz hydrogène et (R) un dispositif d'utilisation de gaz hydrogène qui utilise le gaz hydrogène émis par (2) le dispositif de chauffage de gaz hydrogène et le réservoir de stockage temporaire. L'invention concerne également un dispositif de séchage d'aliment, un dispositif conférant un effet antioxydant et un dispositif de génération d'énergie et d'entraînement à cycle fermé d'hydrogène liquide comprenant le dispositif à cycle fermé d'hydrogène liquide.
PCT/JP2017/004574 2016-12-08 2017-02-08 Dispositif à cycle fermé d'hydrogène liquide WO2018105133A1 (fr)

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
JP2016238102A JP2018093740A (ja) 2016-12-08 2016-12-08 食材乾燥方法及びそれに用いる食材乾燥装置
JP2016-238102 2016-12-08
JP2016006115U JP3209283U (ja) 2016-12-21 2016-12-21 抗酸化作用付与装置
JP2016-006115U 2016-12-21
JP2017-000033U 2017-01-10
JP2017000033U JP3209521U (ja) 2017-01-10 2017-01-10 水素流体閉サイクル駆動・発電装置

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CN111766191A (zh) * 2020-08-10 2020-10-13 盐城新海川机电科技有限公司 一种环保材料筒渗透试验机及其工作方法

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