Compound, production method therefor, and hydrogen supply method

Abstract

One compound (100) according to the present invention contains silicon fine particles having a capability of generating hydrogen or aggregates of the silicon fine particles. The compound that contains the silicon fine particles or the aggregates having a capability of generating hydrogen is capable of generating hydrogen in the body of, for example, an animal that has ingested the compound. For a plant, the compound can be disposed or charged into, for example, moisture (water-containing liquid) or fertilizer to be provided to the plant, to supply the plant with hydrogen generated from the compound.

Claims

1. A medicine for an animal or a human or a feed for a livestock or food for a pet comprising a solid formulation, the solid formulation comprising silicon fine particles having a capability of generating hydrogen or aggregates of the silicon fine particles, wherein the silicon fine particles or the aggregates of the silicon fine particles have surfaces capable of getting direct contact with water of a water-containing medium while retaining hydrophilicity on the surfaces, wherein the silicon fine particles or the aggregates of the silicon fine particles have a heterogeneous or incomplete oxide film on the surfaces, and wherein the silicon fine particles or the aggregates are blended into the solid formulation.

2. The medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 1, wherein the silicon fine particles include silicon fine particles having a crystallite diameter of 1 nm or more and 100 nm or less.

3. The medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 1, further comprising a pH adjusting agent being capable of making the water-containing medium have a pH value of 5 or more, wherein the water-containing medium is in contact with the silicon fine particles or the aggregates.

4. The medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 3, wherein the pH adjusting agent is at least one selected from the group consisting of potassium carbonate, sodium carbonate, sodium hydrogencarbonate, sodium hydroxide, and potassium hydroxide.

5. The medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 3, wherein the medium is at least one selected from the group consisting of a liquid form, a gel form, a cream form, a paste form, an emulsion form, and a mousse form.

6. A hydrogen supply method comprising contacting the medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 1 with the water-containing medium having a pH value of 5 or more, inside or outside of the body of the animal or the human.

7. The hydrogen supply method according to claim 6, wherein the silicon fine particles include silicon fine particles having a crystallite diameter of 1 nm or more and 100 nm or less.

8. The hydrogen supply method according to claim 6, wherein the water-containing medium has a pH value of 6 or more.

9. The medicine for the animal or the human or the feed for the livestock or the food for the pet comprising the solid formulation according to claim 1, wherein the water-containing medium includes in-vivo or ex-vivo water.

10. A medicine, a fertilizer, or a compost for a plant comprising a solid formulation, the solid formulation comprising silicon fine particles having a capability of generating hydrogen or aggregates of the silicon fine particles, wherein the silicon fine particles or the aggregates of the silicon fine particles have surfaces capable of getting direct contact with water of a water-containing medium while retaining hydrophilicity on the surfaces, wherein the silicon fine particles or the aggregates of the silicon fine particles have a heterogeneous or incomplete oxide film on the surfaces, and wherein the silicon fine particles or the aggregates are blended into the solid formulation.

11. The medicine, the fertilizer, or the compost for the plant comprising the solid formulation of claim 10, wherein the water-containing medium includes in-vivo or ex-vivo water.

12. The medicine, the fertilizer, or the compost for the plant comprising the solid formulation of claim 10, further comprising a pH adjusting agent being capable of making the water-containing medium have a pH value of 5 or more, wherein the water-containing medium is in contact with the silicon fine particles or the aggregates.

13. A hydrogen supply method comprising: contacting the medicine, the fertilizer, or the compost for the plant comprising the solid formulation according to claim 10 with the water-containing medium having a pH value of 5 or more.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows photographs ((a) perspective view and (b) side view) of a solid formulation (compound) according to a first embodiment.

(2) FIG. 2 shows a schematic diagram illustrating the relationship between the solid formulation (compound) according to the first embodiment contained in a medium (soil) and a plant (tree).

(3) FIG. 3 shows a side view (a) illustrating a laminate structure of a layered solid formulation and a medium before generation of hydrogen in a modified example (2) of the first embodiment, and a side view (b) of the laminate structure of the layered solid formulation and the medium when hydrogen is generated in the modified example (2) of the first embodiment.

(4) FIG. 3B shows a side view illustrating a structure of a layered solid formulation in a modified example (3) of the first embodiment.

(5) FIG. 4 shows a graph illustrating the amount of hydrogen generated in Examples 1 and 2.

(6) FIG. 5A shows a photograph illustrating a state of a solid formulation in accordance with the first embodiment directly after the solid formulation is brought into contact with pure water.

(7) FIG. 5B shows a photograph illustrating a state of a solid formulation in accordance with the first embodiment about 60 seconds after the solid formulation is brought into contact with pure water.

(8) FIG. 5C shows a photograph illustrating a state of a solid formulation in accordance with a modified example (6) of the first embodiment directly after the solid formulation is brought into contact with pure water.

(9) FIG. 6 shows a graph illustrating the hydrogen generation amount in Examples 3 to 7.

(10) FIG. 7 shows a graph (a) illustrating chronological changes in amount of dissolved hydrogen generated by bringing silicon fine particles prepared under each condition of a second embodiment into contact with an aqueous solution obtained by dissolving sodium hydrogencarbonate in pure water, and a graph (b) illustrating chronological changes in hydrogen generation amount per 1 g of the silicon fine particles of the second embodiment.

DESCRIPTION OF REFERENCE SIGNS

(11) 20: Base 70: Film 90a: Soil 90b: Medium 100: Solid formulation 100a: Layered solid formulation 200: Laminate structure

EMBODIMENTS OF THE INVENTION

(12) Embodiments of the present invention will be described in detail with reference to the accompanying drawings.

First Embodiment

(13) Silicon fine particles (or aggregates thereof) according to the present embodiment and a compound according to the present embodiment have a capability of generating hydrogen. The compound according to the present embodiment contains the aggregates or the silicon fine particles (typically having a crystallite diameter of 1 nm or more and 100 nm or less) having a capability of generating hydrogen. Hereinafter, silicon fine particles (or aggregates thereof) and a solid formulation (compound) containing the silicon fine particles (or the aggregates) will be described in detail as one example of the compound according to the present embodiment. In addition, a hydrogen supply method according to the present embodiment will be also described in detail.

(14) [1] Silicon Fine Particles (or Aggregates Thereof) and Solid Formulation, and Production Method for Silicon Fine Particles (or Aggregates Thereof) and Solid Formulation

(15) The solid formulation according to the present embodiment is produced using silicon fine particles (hereinafter, also referred to as “silicon nanoparticles” for the sake of convenience) including, as main particles, silicon nanoparticles obtained by finely dividing, according to a bead mill method, a commercially available high-purity silicon particle powder (typically, manufactured by Kojundo Chemical Laboratory Co., Ltd., particle diameter distribution: <φ5 μm (but silicon particles having a crystal grain diameter of more than 1 μm, purity: 99.9% i-type silicon) as silicon particles. The present embodiment employs a step of grinding silicon particles in ethanol solution to form the silicon fine particles or aggregates of the silicon fine particles.

(16) Specifically, 200 g of the high-purity silicon powder id dispersed in 4 L (liters) of a 99.5 wt % ethanol solution, φ0.5 μm zirconia beads (volume: 750 ml) are added, and the mixture is finely divided by performing grinding (one-step grinding) at a rotation speed of 2500 rpm for 4 hours using a bead mill apparatus (manufactured by AIMEX CO., Ltd. horizontal continuous ready mill, (model: RHM-08).

(17) In the present embodiment, a separation slit provided in a grinding chamber of the bead mill apparatus separates the mixture into the beads and an ethanol solution containing silicon nanoparticles. The ethanol solution containing silicon nanoparticles that has been separated from the beads is heated to 30° C. to 35° C. with a vacuum evaporator. As a result, the ethanol solution is evaporated to give the silicon nanoparticles and/or aggregates thereof.

(18) The silicon fine particles obtained by the above-mentioned method mainly include silicon nanoparticles having a crystallite diameter of 1 nm or more and 100 nm or less. More specifically, as a result of measuring the silicon nanoparticles by an X-ray diffractometer (SmartLab manufactured by Rigaku Corporation), the following values were obtained as one example. In a volume distribution, the mode diameter was 6.6 nm, the median diameter was 14.0 nm, and the average crystallite diameter was 20.3 nm.

(19) The silicon nanoparticles were observed using a scanning electron microscope (SEM), and the result showed that the silicon nanoparticles were partially aggregated to form slightly large formless aggregates with about 0.5 μm or less. In addition, individual silicon nanoparticles were observed using a transmission electrode microscope (TEM), and the result showed that main silicon nanoparticles had a crystallite diameter of about 2 nm or more and 20 nm or less.

(20) Thereafter, a first mixing step of mixing hydrogen peroxide water with the silicon nanoparticles in a glass container (hereinafter, also referred to as a “H.sub.2O.sub.2 treatment” or a “hydrogen peroxide water treatment step”) is performed in the present embodiment. In the present embodiment, the temperature of the hydrogen peroxide water (3.5 wt % in the present embodiment) in the mixing step is 75° C. The mixing time is 30 minutes. Sufficient stir in the first mixing step (hydrogen peroxide water treatment step) is preferred to increase the opportunity of the silicon nanoparticles getting in contact with the hydrogen peroxide water. Even when the temperature of the hydrogen peroxide water in the first mixing step (hydrogen peroxide water treatment step) is, for example, about room temperature, at least a part of the effects of the present embodiment can be exhibited.

(21) The silicon nanoparticles mixed with the hydrogen peroxide water are subjected to a solid-liquid separation treatment using a known centrifugal separator to remove the hydrogen peroxide water and thus give silicon nanoparticles. As a result, it is possible to obtain silicon nanoparticles having their surfaces treated with hydrogen peroxide water. Here, the treatment of the surfaces of the silicon nanoparticles with hydrogen peroxide water is capable of removing an alkyl group (e.g. a methyl group) present on the surfaces of the silicon nanoparticles. As a result, the silicon nanoparticles (and silicon file particles including, as main particles, the silicon nanoparticles) and aggregates thereof are capable of forming a state in which they have surfaces capable of getting direct contact with a medium capable of containing a water-containing liquid, while as a whole retaining hydrophilicity on their surfaces. Such a special surface treatment is capable of promoting the generation of hydrogen with higher accuracy.

(22) Thereafter, a second mixing step of mixing the silicon nanoparticles with an ethanol solution is further performed in the present embodiment. Sufficient stir in the mixing step is preferred to increase the opportunity of the silicon nanoparticles getting in contact with the ethanol solution (99.5 wt % in the present embodiment). The silicon nanoparticles mixed with the ethanol solution are subjected to a solid-liquid separation treatment using a known centrifugal separator for removal of the ethanol solution that is highly volatile and then sufficiently dried to produce one type of final silicon nanoparticles according to the present invention.

(23) In the present embodiment, as another type of final silicon nanoparticles, silicon nanoparticles were also produced, with the mixing time of the hydrogen peroxide water with the silicon nanoparticles set to 60 minutes in the first mixing step of the above-described steps. Another aspect of the present embodiment also includes appropriate control of the shape and the structure of the silicon fine particles and the aggregates thereof.

(24) The present embodiment does not use an isopropyl alcohol solution unlike a second embodiment described later but uses the ethanol solution and the hydrogen peroxide water, and thus, it is worth noting that it is possible to provide a solid formulation (compound) capable of playing a role as a hydrogen supply material that is safer and more secure for a living body, a production method for the solid formulation (compound), and a hydrogen supply method.

(25) The silicon nanoparticles in an amount of 5 mg are mixed with 495 mg of a sodium hydrogencarbonate powder (manufactured by Wako Pure Chemical Industries, Ltd., purity: 99.5%). The mixture is kneaded and formed into a substantially columnar lump body having a diameter of about 5 mm and a height of about 10 mm by a tableting method to give a solid formulation (compound) 100 shown in FIG. 1. FIG. 1(a) is a perspective view of the solid formulation (compound) 100 as one example, and FIG. 1(b) is a side view of the solid formulation (compound) 100 as the one example. One employable aspect is also an aspect in which the silicon fine particles (including aggregates thereof) not formed into a solid formulation (e.g. in a powder form) or aggregates of the silicon fine particles are contained in a “base material” such as a medicine for an animal, food for livestock or a pet, or feed for an animal, or a medicine for a plant, fertilizer for a plant, or compost for a plant, described later.

(26) [2] Medium

(27) Next, one employable aspect of the present embodiment is also preparing a “medium” with which the silicon nanoparticles (or the aggregates thereof) or the solid formulation (compound) 100 is brought into contact.

(28) A material or a commercial product for the “medium” in the present embodiment is not particularly limited. One example of the medium is a water-containing liquid (including only water) present in the body of an animal. Another example of the medium is a medium that allows an animal (including a fish) or a plant to dermally or transmucosally take hydrogen in its body and is physiologically acceptable. Such a medium can allow at least a part of the effects of the present embodiment to be exhibited. One example of a site for taking hydrogen in the body is the skin itself or the mucous membrane itself for the case of an animal and a leaf, a stem, a cortex, or a root for the case of a plant.

(29) A suitable example of the medium is at least one selected from the group consisting of a liquid form, a gel form, a cream form, a paste form, an emulsion form, and a mousse form, in terms of increasing the opportunity of a site of an animal or a plant getting contact with a water-containing liquid or a medium containing the water-containing liquid (hereinafter, also referred to collectively as a “medium”). Other suitable examples of the medium include soil containing rainwater or artificial water, an artificial shower that sprays water, an artificial pond, a puddle (including a naturally formed puddle), water in a preserve for farming fishes and shellfishes (including crustaceans; the same applies hereinafter) or seaweed, and water in an aquarium for fishes and shellfishes or seaweed. Therefore, in one example of the present embodiment, the production method for a medium is artificially producing the soil, the shower, the pond, or the puddle with use of known means. In any example, the medium is preferred to be alkaline in terms of promoting the generation of hydrogen.

(30) As one example, the solid formulation (compound) 100 is as shown in FIG. 2, buried in soil (containing moisture) 90a in which a plant (tree) is planted or naturally grown, to utilize the soil 90a as the medium in the present embodiment. The solid formulation (compound) 100 is brought into contact with the soil 90a as the medium to generate hydrogen (H.sub.2). As a result, it is possible for the tree in contact with the soil 90a to take hydrogen in its body through its root or cortex. As a result, it is possible to attain prevention or suppression of photosynthesis inhibition, leaf discoloration, growth promotion, and/or withering of a plant. Some plants are also capable of attaining an increase in sugar content. A typical example of the moisture in the present embodiment is rainwater or artificial water. The number or the amount of the solid formulation (compound) in the soil 90a is not particularly limited.

(31) Although not shown in a drawing, another employable aspect of the present embodiment is also introducing or charging the solid formulation (compound) 100 into a naturally present or artificial puddle (medium) to bring the solid formulation (compound) 100 into contact with the water-containing liquid. The solid formulation (compound) 100 is brought into contact with the water-containing liquid to generate hydrogen (H.sub.2). In this aspect, an animal gets contact with or is immersed in the puddle to be capable of taking hydrogen in its body through the water-containing liquid. As a result, hydrogen directly, or dermally or transmucosally taken in the body is capable of appropriately eliminating, removing, or reducing excess active oxygen (particularly hydroxyl radicals) in the body of the animal, so that it is possible to attain health promotion and/or disease prevention of the animal.

(32) If the puddle has a pH value higher than weak activity (e.g. a pH value of 5 or more), the presence of sodium hydrogencarbonate containing the solid formulation (compound) 100 according to the present embodiment increases, as described later, the pH value to allow the puddle to satisfy the condition as the medium that allows easy generation of hydrogen (H.sub.2). In other words, when the water-containing liquid such as a puddle is acidic, many solid formulations (compounds) 100 are required to be introduced or charged into the soil 90a to make the water-containing liquid satisfy the condition as the medium that allows easy generation of hydrogen (H.sub.2).

(33) The solid formulation (compound) 100 according to the present embodiment contains sodium hydrogencarbonate. Therefore, even when the soil 90a or the puddle as the medium is neutral or weakly acidic, the solid formulation (compound) 100 is buried, introduced, or charged into the soil 90a or the puddle as the medium to undergo a contact step of bringing the silicon fine particles or the aggregates thereof according to the present embodiment into contact with the medium. As a result, it is possible to change, for example, the soil 90a or the puddle to a weakly acidic medium having a pH value of 6 or more, more suitably a basic medium having a pH value of more than 7 and thus to promote the generation of hydrogen (H.sub.2).

(34) Therefore, it is possible to bring hydrogen (H.sub.2) generated by the contact step into contact with the skin and/or the mucous membrane of an animal or with a leaf, a stem, a cortex, and/or a root of a plant through the soil 90a or the puddle as the medium. As a result, the present embodiment allows an animal or a plant to take hydrogen (H.sub.2) in its body.

(35) As described above, for example, the soil 90a or the puddle plays a role as the medium in the present embodiment. As a result, an animal is capable of taking hydrogen (H.sub.2) in its body from its skin or mucous membrane through the medium or directly. A plant is capable of taking hydrogen (H.sub.2) in its body from its leaf, stem, cortex, or root through the medium or directly.

(36) In the present embodiment, the solid formulation (compound) 100, or the silicon fine particles (including the aggregates thereof) not formed into the solid formulation or the aggregates of the silicon fine particles are not limited to cases in which they are used as they are. One employable preferred aspect is also an aspect in which the solid formulation (compound) 100, or the silicon fine particles (including the aggregates thereof) not formed into the solid formulation or the aggregates of the silicon fine particles are contained in the “base material” such as a medicine for an animal, food for livestock or a pet, or feed for an animal, or a medicine for a plant, fertilizer for a plant, or compost for a plant. For example, one typical example is mixing or kneading as an additive, for example, 0.1 wt % to 50 wt % of the solid formulation 100, or the silicon fine particles (including the aggregates thereof) not formed into the solid formulation or the aggregates of the silicon fine particles, with the base material. Therefore, the “base material” is also the “compound” in a broad sense in the present invention as containing the solid formulation 100, or the silicon fine particles (including the aggregates thereof) not formed into the solid formulation or the aggregates of the silicon fine particles. Therefore, bringing such a base material into contact with the medium is employable as preferred means for allowing an animal or a plant to take hydrogen in its body, for example, dermally or transmucosally.

(37) In addition, if the solid formulation (compound) according to the present embodiment does not contain sodium hydrogencarbonate, for example, the soil 90a or the puddles having a pH value of 5 or more is capable of satisfying the condition as the medium that allows easy generation of hydrogen (H.sub.2). The pH value is more suitably 6 or more (or more than 6), further suitably 7 or more (or more than 7) in terms of attaining a medium that allows easy generation of hydrogen (H.sub.2) with higher accuracy. The pH value is further suitably more than 7.4, very suitably more than 8).

Modified Example (1) of First Embodiment

(38) In the compound and the hydrogen supply method according to the first embodiment, one preferred aspect is further including an introduction step of introducing a “pH adjusting agent” into the medium or the “base material,” for adjusting the pH value of the soil 90a or the puddle in the first embodiment to make the soil or the puddle satisfy the condition for easier generation of hydrogen, in other words, to make the pH value of the soil or the puddle fall within the numerical range for easier generation of hydrogen.

(39) The sodium hydrogencarbonate in the first embodiment is one example of the “pH adjusting agent,” but the “pH adjusting agent” is not limited to sodium hydrogencarbonate. Therefore, the material for the “pH adjusting agent” is not limited as long as it is a material (hereinafter, also referred to as a “weak acidic agent”) capable of adjusting the medium or the base material to weak acidity, or a pH value of 5 or more or 6 or more (or more than 6), or it is a material (hereinafter, also referred to as an “alkaline agent”) capable of adjusting the medium or the base material to alkaline, or a pH value of more suitably 7 or more (or more than 7) (more suitably more than 7.4, further suitably more than 8). A typical example of the weak acidic agent is at least one acid or a salt thereof selected from the group consisting of citric acid, gluconic acid, phthalic acid, fumaric acid, and lactic acid. A typical example of the alkaline agent is at least one selected from the group consisting of potassium carbonate, sodium carbonate, sodium hydrogencarbonate, sodium hydroxide, and potassium hydroxide. The most suitable alkaline agent is sodium hydrogencarbonate in terms of physiology. This is because sodium hydrogencarbonate is widely used as a food additive and has a plurality of advantages such as a pH value adjustment function required in the present embodiment and excellent safety and versatility.

Modified Example (3) of First Embodiment

(40) As another modified example of the first embodiment, the solid formulation (compound) according to the first embodiment can be formed in layers to form a laminate structure 200 of a layered solid formulation (compound) and a medium. FIG. 3A(a) shows a side view illustrating the laminate structure 200 of the layered solid formulation and the medium before generation of hydrogen, and FIG. 3A(b) shows a side view illustrating the laminate structure 200 of the layered solid formulation and the medium when hydrogen is generated.

(41) As shown in FIGS. 3A(a) and 3A(b), the laminate structure 200 includes at least a layered solid formulation 100a and a medium 90b on or above a base 20 (e.g. fiber, a natural resin, a synthetic resin, metal, a semiconductor, ceramics, or glass). Here, as already described, a suitable example of the medium 90b is a material that is physiologically acceptable and is at least one selected from the group consisting of a liquid form, a gel form, a cream form, a paste form, an emulsion form, and a mousse form. The base 20 is not necessarily provided when the laminate structure 200 of the layered solid formulation and the medium can be held without particularly providing the base 20.

(42) As shown in FIG. 3A(a), in a stage before generation of hydrogen, an impermeable film 70 is provided between the layered solid formulation (compound) 100a and the medium 90b so as not to allow the layered solid formulation (compound) 100a to get contact with the medium 90b. A film formed of a known impermeable material can be utilized as the film 70. For example, an example of the material for the impermeable film 70 is a polymer such as known polyethylene. As another example, one employable aspect is also employment of a water-disintegrable and impermeable sheet disclosed in International Publication No. WO 2011/036992.

(43) On the other hand, as shown in FIG. 3A(b), drawing the film 70 in the arrow direction at least partially brings the layered solid formulation 100a into direct contact with the medium 90b. As a result, the layered solid formulation (compound) 100a can get contact with the medium 90b capable of containing a water-containing liquid having a pH value of 7 or more to generate hydrogen in cooperation with the pH adjusting agent typified by sodium hydrogencarbonate.

(44) The present embodiment forms the structure so that drawing the film 70 in the arrow direction (toward the left on the paper) brings the layered solid formulation (compound) 100a into direct contact with the medium 90b. The method of removing the film 70, however, is not particularly limited. For example, one employable aspect is formation of the structure so that the medium 90b is brought into contact with the silicon fine particles (the layered solid formulation (compound) 100a in the present embodiment) or the aggregates thereof when at least a part of the film 70 is removed or dissolved. As regards an example of the material for dissolving at least a part of the film 70, one employable aspect is also employment of a water-disintegratable and impermeable sheet disclosed in International Publication No. WO 2011/036992. Another employable aspect is also covering with the impermeable film 70 the solid formulation (compound) 100 according to the first embodiment in place of the layered solid formulation (compound) 100a in a stage before generation of hydrogen. When removal or dissolution of the film 70 at least partially brings the solid formulation (compound) 100 into direct contact with the medium 90b, the same effects as those in the layered solid formulation (compound) 100a can be exhibited.

(45) When the medium is, for example, at least one selected from the group consisting of a liquid form, a gel form, a cream form, a paste form, an emulsion form, and a mousse form, the two layers (the layered solid formulation (compound) 100a and the medium 90b) shown in FIG. 3A(b) are considered not to possibly retain a state of being clearly separated from each other. Such a case increases the contact area between the layered solid formulation (compound) 100a and the medium 90b and is thus rather preferred in terms of promoting the generation of hydrogen with higher accuracy.

Modified Example (3) of First Embodiment

(46) As another modified example of the first embodiment, another employable aspect is also a layered solid formulation (compound) produced by forming the solid formulation (compound) according to the first embodiment in layers. A structure 200a as one example shown in FIG. 3B includes a layered solid formulation (compound) 100a on a base 20. The base 20 is not necessarily provided when the shape of the layered solid formulation (compound) can be held without particularly providing the base 20. The impermeable film 70 shown in the modified example (2) of the first embodiment may be provided so as to cover the layered solid formulation (compound) 100a, in terms of highly accurately avoiding contact with moisture in air.

(47) As shown in FIG. 3B, one preferred aspect of the present embodiment is, for example, bringing the layered solid formulation (compound) 100a into contact with the animal skin or mucous membrane and then into contact with moisture-containing sweat or body fluid from the skin or mucous membrane to generate hydrogen. Such a case also allows an animal to take hydrogen in its body in the same manner as in the modified example (2) of the first embodiment. It is possible to supply, as the moisture, water (e.g. clean water) in place of the sweat or the body fluid by, for example, spraying before (e.g. directly before) using the layered solid formulation (compound) 100a.

(48) It is worth noting that the structures of the laminate structures of the present embodiment are employable structures in various “scenes.” For example, typical commercial products that can employ (possibly include) the medium are exemplified by the following items (1) to (3):

(49) (1) one washing agent selected from the group consisting of shampoo for an animal and soap for an animal;

(50) (2) one therapeutic material selected from the group consisting of ointment and fomentation; and

(51) (3) one hygienic material selected from the group consisting of a water-absorbent resin, water-absorbent nonwoven fabric, water-absorbent fiber, water-absorbent felt, and water-absorbent gel (or gelled agent).

(52) Here, the “hygienic material” includes hygienic gloves, a head cover, a head band, a bed pad, a bed sheet, a clothing item, a wound treatment product (including a wound covering material, tape, and a bandage), a disposable diaper, gauze, a gown, a hygienic tissue (including a wet towel, a face washing towel, a patch, a wet tissue, and a napkin), absorbent cotton, a cotton swab, adhesive-plaster, and surgical tape.

Modified Example (4) of First Embodiment

(53) As another modified example of the first embodiment, 4 g of citric acid (manufactured by Wako Pure Chemical Industries, Ltd., purity: 99.5%) is further added to 2 g of the silicon nanoparticles and 34 g of the sodium hydrogencarbonate powder that are used in the first embodiment, and the mixture is kneaded to form a substantially columnar lump body having a diameter of about 5 mm and a height of about 10 mm, so that the same solid formulation (compound) as the solid formulation (compound) 100 shown in FIG. 1 can be obtained.

Modified Example (5) of First Embodiment

(54) As another modified example of the first embodiment, a solid formulation is obtained by the same treatments as in the modified example (4) of the first embodiment except that the amounts of the sodium hydrogencarbonate powder and citric acid are changed to 19 g and 19 g, respectively. This solid formulation (compound) is the same substantially columnar solid formulation (compound) as the solid formulation (compound) 100 shown in FIG. 1 and has a diameter of about 5 mm and a height of about 10 mm. The mixing ratio among citric acid, sodium hydrogencarbonate, and the silicon nanoparticles can be appropriately changed.

Modified Example (6) of First Embodiment

(55) In the present embodiment, the same high-purity silicon particle powder as that used in the first embodiment (typically, silicon particles having a crystal grain diameter of more than 1 μm) is ground in one step by the procedures described in the first embodiment. In the present embodiment, the φ0.5 μm zirconia beads (volume: 750 ml) used in the one-step grinding are automatically separated from a solution containing silicon nanoparticles in a bead mill grinding chamber. Further φ0.3 μm zirconia beads (volume: 300 mml) are added to the solution containing silicon nanoparticles from which the beads have been separated, and the mixture is finely divided by performing grinding (two-step grinding) at a rotation speed of 2500 rpm for 4 hours.

(56) The silicon nanoparticles including the beads are separated from the solution containing silicon nanoparticles as described above. The ethanol solution containing silicon nanoparticles that has been separated from the beads is heated to 40° C. using a vacuum evaporator in the same manner as in the first embodiment for solution evaporation of ethanol to give the silicon nanoparticles.

Modified Example (7) of First Embodiment

(57) Another employable aspect is also further providing a physiologically acceptable covering layer that covers the solid formulation (compound) 100 according to the first embodiment or the solid formulations (compounds) described in the modified examples (4) and (5) of the first embodiment. For example, it is possible to employ a known coating agent (e.g. a known enteric material hardly soluble in the stomach) that covers the outermost layer of the solid formulation (compound) 100. An example of a physiologically acceptable covering layer applicable as a capsule preparation is a capsule which encapsulates the silicon fine particles (mainly the aggregates of the silicon fine particles) or the aggregates thereof and is produced from a known material (e.g. a known enteric material hardly soluble in the stomach). When the solid formulation (compound) 100 is employed, a disintegrating agent may be further included. For the disintegrating agent, a known material is employable. In addition, a preferred example of a more suitable disintegrating agent is an organic acid, and the most suitable example is citric acid. Here, the organic acid can also function as a binding agent that brings the silicon nanoparticles into a lump form.

(58) The temperature condition is not particularly limited for the water-containing liquid for generating hydrogen or the medium capable of containing the water-containing liquid in the embodiments. The temperature of the medium that allows the generation of hydrogen, however, is higher than 0° C. and 50° C. or lower. The water-containing liquid or the medium having a temperature of suitable 20° C. (more suitably 25° C.) or higher and 50° C. or lower promotes the reaction of generating hydrogen. Further, the water-containing liquid or the medium having a temperature of 35° C. or higher and 50° C. or lower promotes the generation of hydrogen with higher accuracy. An upper limit of the temperature of the water-containing liquid or the medium is not particularly limited as long as an animal or a plant is not wound or damaged.

(59) Hereinafter, the embodiments will be described in more detail by way of examples, but the embodiments are not limited to these examples.

Example 1

(60) The present inventors checked the state of generation of hydrogen without performing a tableting step by a tableting method, to evaluate silicon nanoparticles themselves. Specifically, an experiment was conducted as Example 1, using silicon nanoparticles subjected to the one-step grinding in the first embodiment.

(61) The silicon nanoparticles described in the first embodiment in an amount of 10 mg and in a form of a powdered preparation (i.e. the silicon nanoparticles were not either mixed or kneaded with a sodium hydrogencarbonate powder) were poured into a glass bottle having a volume of 100 ml (borosilicate glass having a thickness of about 1 mm, LABORAN Screw Tubular Bottle manufactured by AS ONE Corporation). Tap water having a pH value of 7.1 in an amount of 30 ml was poured into the glass bottle, the glass bottle was hermetically sealed under the temperature condition of a liquid temperature of 25° C., the concentration of hydrogen in the liquid in the glass bottle was measured, and the hydrogen generation amount was determined using the measured concentration of hydrogen. For measurement of the concentration of hydrogen, a portable dissolved hydrogen meter (Model: DH-35A manufactured by DKK-TOA CORPORATION) was used.

Example 2

(62) Example 2 was conducted in the same manner as Example 1 except that 30 ml of tap water was poured and the temperature condition was changed to a liquid temperature of 37° C.

(63) FIG. 4 shows the results of Examples 1 and 2. In FIG. 4, the absicca represents the time (min) during which the solid formulations (compound) was kept in contact with the water-containing liquid, and the ordinate of the graph represents the hydrogen generation amount.

(64) As shown in FIG. 4, the generation of hydrogen was confirmed even when nearly neutral water was brought into contact with the silicon nanoparticles described in the first embodiment. It was clarified that a high liquid temperature increases the hydrogen generation amount. Particularly, it was confirmed that when the liquid temperature is 37° C. close to human body temperature, the generation of hydrogen is attained in a shorter time and a great amount (1.5 ml/g or more) of a hydrogen is continuously generated thereafter.

(65) In addition to the results of Examples 1 and 2, the present inventors conducted the evaluations indicated in Example 3 and the following examples for the various solid formulations (compound) that were processed by a tableting method and are described in the first embodiment and the modified examples thereof.

Example 3

(66) Employed as a sample for Example 3 was a solid formulation (compound) having one-fifth (φ10×1.6 mm, silicon nanoparticles: 16 mg, sodium hydrogencarbonate: 304 mg) the diameter and the height of one solid formulation (compound) 100 produced by the treatments described in the first embodiment.

(67) The sample was placed in a stainless container having a volume of 60 ml. Pure water (pH value: 7.0) as an example of the water-containing liquid in an amount of 60 ml was poured into the stainless container to immerse the solid formulation (compound) in the pure water, and the liquid temperature was kept at 25° C. Under this condition, the glass bottle was hermetically sealed, the concentration of hydrogen in hydrogen water produced in the glass bottle was measured using the meter described in Example 1, and the hydrogen generation amount was determined.

(68) The solid formulation (compound) gradually disintegrated its shape in the pure water with elapse of time. Sodium hydrogencarbonate was dissolved in the liquid with elapse of time after the solid formulation (compound) was brought into contact with the pure water, and the silicon nanoparticles were partially settled and left on the bottom of the container while almost uniformly diffused in the liquid. As a result, the solid formulation (compound) hardly retained its original shape and assumed a powdery form (or a fine powdery form; hereinafter, referred to collectively as a “powdery form”) (hereinafter, a phenomenon in which the form of a solid formulation is disintegrated into a powdery form is referred to as “disintegration.” Dissolution of a capsule of a capsule preparation encapsulating a powder also means that the form of a formulation is disintegrated, and exposure of a powder by dissolution of a capsule is also encompassed in “disintegration”). In this example, sodium hydrogencarbonate released with disintegration of the solid formulation (compound) was dissolved in water, and therefore the pH value of the water-containing liquid in the glass bottle increased to 8.3.

Example 4

(69) Example 4 as a sample a solid formulation (compound) having one-fifth (φ10×1.6 mm, silicon nanoparticles: 16 mg, sodium by hydrogencarbonate: 272 mg, citric acid: 32 mg) the diameter and the height of the solid formulation (compound) produced by the treatments described as the modified example (4) of the first embodiment. The solid formulation (compound) was almost wholly disintegrated into a powdery form about 5 minutes after brought into contact with pure water under the temperature condition of a liquid temperature of 25° C. In the process of disintegration of the solid formulation (compound) (i.e. until 90 minutes after the solid formulation (compound) was brought into contact with pure water), sodium hydrogencarbonate and citric acid were released with disintegration of the solid formulation (compound), so that the water-containing liquid had a pH value of 7.6.

Example 5

(70) Example 5 employed, as a sample, a solid formulation (compound) having one-fifth (φ10×1.6 mm, silicon nanoparticles: 16 mg, sodium hydrogencarbonate: 152 mg, citric acid: 152 mg) the diameter and the height of the solid formulation (compound) prepared by the procedures described as the modified example (5) of the first embodiment. The solid formulation (compound) was almost wholly disintegrated into a powdery form about 5 minutes after brought into contact with pure water under the temperature condition of a liquid temperature of 25° C. In the process of disintegration of the solid formulation (compound) (i.e. until 90 minutes after the solid formulation (compound) was brought into contact with pure water), sodium hydrogencarbonate and citric acid were released with disintegration of the solid formulation (compound), so that the water-containing liquid had a pH value of 6.0.

Example 6

(71) Example 6 employed, as a sample, a solid formulation (compound) having one-fifth (φ10×1.6 mm, silicon nanoparticles: 16 mg, sodium hydrogencarbonate: 272 mg, citric acid: 32 mg) the diameter and the height of the solid formulation (compound) prepared by the procedures described as the modified example (6) of the first embodiment. The stainless container was held in a thermostatic bath to keep the liquid temperature at 37° C. As the water-containing liquid, pure water having a pH value of 7.0 was used. The solid formulation (compound) was almost wholly disintegrated into a powdery form about 5 minutes after brought into contact with pure water. Sodium hydrogencarbonate and citric acid were released with disintegration of the solid formulation (compound), so that the water-containing liquid had a pH value of 7.6.

Example 7

(72) Example 7 as a sample a solid formulation (compound) having one-fifth (φ10×1.6 mm, silicon nanoparticles: 16 mg, sodium by hydrogencarbonate: 152 mg, citric acid: 152 mg) the diameter and the height of the solid formulation (compound) produced by the treatments described in the modified example (7) of the first embodiment. The stainless container was held in a thermostatic bath to keep the liquid temperature at 37° C. As the water-containing liquid, pure water having a pH value of 7.0 was used. The solid formulation (compound) was almost wholly disintegrated into a powdery form about 5 minutes after brought into contact with pure water. Sodium hydrogencarbonate and citric acid were released with disintegration of the solid formulation (compound), so that the water-containing liquid had a pH value of 6.0.

(73) In the examples, it is possible to confirm by visual inspection how the solid formulation (compound) gradually disintegrates its shape in pure water with elapse of time. One example of how the solid formulation (compound) is disintegrated is shown by FIGS. 5A and 5B that are photographs illustrating how a solid formulation (compound) (an example in accordance with the first embodiment) formed using 2 g of the silicon nanoparticles and 38 g of sodium hydrogencarbonate behaves with elapse of time when charged into 500 ml of pure water. FIG. 5A illustrates the state of the solid formulation (compound) directly after the solid formulation (compound) was brought into contact with pure water. FIG. 5B illustrates the state of the solid formulation (compound) about 60 seconds after the solid formulation (compound) was brought into contact with pure water.

(74) On the other hand, FIG. 5C shows a photograph illustrating the state of a solid formulation (compound) (an example in accordance with the modified example (6) of the first embodiment) formed using 2 g of the silicon nanoparticles, 19 g of sodium hydrogencarbonate, and 19 g of citric acid, directly after the solid formulation (compound) was brought into contact with pure water.

(75) As shown by FIGS. 5A to 5C, it was confirmed that when the solid formulation (compound) was brought into contact with pure water, sodium hydrogencarbonate was dissolved in the liquid with elapse of time, and the silicon nanoparticles were partially settled and left on the bottom of the container while almost uniformly diffused in the liquid.

(76) FIG. 6 shows the results of Examples 3 to 7. In FIG. 6, the abscissa represents the time (min) during which the solid formulation (compound) was kept in contact with the water-containing liquid, and the ordinate of the graph represents the hydrogen generation amount.

(77) In Example 3, the solid formulation (compound) disintegrated its form to release sodium hydrogencarbonate as shown in FIGS. 5A and 5B. The hydrogen generation amount increased with elapse of contact time between the solid formulation (compound) and the water-containing liquid as shown in FIG. 6.

(78) In comparison of Example 3 with Example 5 and comparison of Example 4 with Example 6, the hydrogen generation amount increased under a temperature condition of 37° C. close to human body temperature. Specifically, it is worth noting that Examples 3 and 6 were confirmed to be capable of generating 20 ml/g or more of hydrogen in 240 minutes (four hours).

(79) Further, in comparison of the results of Examples 1, 2, and 6 in which the silicon nanoparticles retaining a powdery form were brought into contact with the water-containing liquid, with the results of Examples 3 to 5 and 7 in which the silicon nanoparticles were used as a solid formulation (compound), it was clarified that the silicon nanoparticles retaining a powdery form are capable of generating more hydrogen when brought into contact with the water-containing liquid, particularly until a certain time (e.g. one and a half hours) after the silicon nanoparticles are brought into contact with the water-containing liquid.

(80) Experiment of Measuring Amount of Hydrogen Generated by Contact Between Silicon Nanoparticles and Medium>

(81) The present inventors also checked chronological changes in amount of hydrogen generated by bringing the silicon fine particles (not the solid formulation (compound)) prepared under each condition of the present embodiment into contact with an aqueous solution obtained by dissolving sodium hydrogencarbonate in pure water.

(82) Specifically, 11 mg of the silicon nanoparticles (first mixing step: 30 minutes) or 5 mg of the silicon nanoparticles (first mixing step: 60 minutes) are mixed in a glass container with an aqueous solution having sodium hydrogencarbonate (1.88 wt %) dissolved therein. The aqueous solution has a pH of about 8.3. Thereafter, the glass container was filled to its opening with the aqueous solution and covered with a lid so as not to allow entry of air for complete hermetic sealing.

(83) The lid was made of polypropylene, but a multilayer filter of polyethylene and polypropylene was used as an inner lid to enable sufficient inhibition of transmission and leakage of generated hydrogen. Some time later after the hermetic sealing, the silicon fine particles prepared under each condition of the present embodiment are confirmed from their appearance and by visual inspection to have been evenly mixed in the whole aqueous solution.

(84) FIG. 7(a) shows a graph illustrating chronological changes in concentration of dissolved hydrogen generated by bringing the silicon fine particles (not the solid formulation (compound)) prepared under each condition of the present embodiment into contact with an aqueous solution obtained by dissolving sodium hydrogencarbonate in pure water. FIG. 7(b) shows a graph illustrating chronological changes in hydrogen generation amount per 1 g of the silicon fine particles prepared under each condition. The graphs show for reference the results of using the silicon fine particles not subjected to the first mixing step. The amounts of dissolved hydrogen were measured using a portable dissolved hydrogen meter (manufactured by DKK-TOA CORPORATION, model: DH-35A).

(85) As shown in FIGS. 7(a) and 7(b), it was clarified that the first mixing step promotes the generation of hydrogen. Particularly, as shown in FIG. 7(b), it is worth noting that the first mixing step is performed to continuously give a hydrogen generation amount of 40 ml or more in 2 hours after elapse of 2 hours from the start of generation of hydrogen.

(86) Meanwhile, the hydrogen generation amount of the silicon fine particles subjected to the first mixing step with a mixing time of 60 minutes is considered to be smaller than the hydrogen generation amount of the silicon fine particles with a mixing time of 30 minutes due to the difference in thickness of an oxide film on the surfaces of the silicon fine particles. That is, it is considered that the silicon fine particles subjected to the first mixing step with a mixing time of 60 minutes had a thicker oxide film to make their direct contact with the medium (aqueous solution) difficult and thus to inhibit the generation of hydrogen.

(87) According to further research and analyses by the present inventors, the silicon fine particles an attain sufficient surface areas capable of getting direct contact with the medium, while appropriately retaining hydrophilicity of the surfaces thereof, when subjected to the first mixing step with a mixing time of more than 2 minutes and 50 minutes or less (more suitably 3 minutes or more and 40 minutes or less, further suitably 4 minutes or more and 30 minutes or less, most suitably 5 minutes or more and 20 minutes or less). As a result, the generation of hydrogen can be more accurately promoted with the mixing time fallen within the above range.

Second Embodiment

(88) Silicon fine particles (or aggregates thereof) according to the present embodiment and a compound according to the present embodiment have a capability of generating hydrogen as in the first embodiment. The compound according to the present embodiment contains silicon fine particles (or aggregates thereof) having a capability of generating hydrogen. The present embodiment is substantially the same as the first embodiment in regard to the compound and the hydrogen supply method except that an isopropyl alcohol (IPA) solution is employed in place of the ethanol solution employed in the first embodiment, so that duplicate description can be omitted.

(89) [1] Silicon Fine Particles (or Aggregates Thereof) and Solid Formulation, And production Method for Silicon Fine Particles (or Aggregates Thereof) and Solid Formulation

(90) Hereinafter, silicon fine particles (or aggregates thereof) and a solid formulation (compound) containing the silicon fine particles (or the aggregates) will be described in detail as one example of the compound according to the present embodiment. In addition, a hydrogen supply method according to the present embodiment will be also described in detail.

(91) For the solid formulation (compound) according to the present embodiment, silicon fine particles (hereinafter, also referred to as “silicon nanoparticles” for the sake of convenience) are used that include as main particles, silicon nanoparticles obtained by finely dividing according to a bead mill method, a commercially available high-purity silicon particle powder (typically, manufactured by Kojundo Chemical Co., Ltd., particle diameter distribution: <φ5 μm, purity: 99.9%, i-type silicon) as silicon particles.

(92) Specifically, 15 g of a high-purity Si powder is dispersed in 300 ml of a 99% or more isopropyl alcohol (IPA) solution, φ0.5 μm zirconia beads (volume: 300 ml) are added, and the mixture is finely divided by performing grinding (one-step grinding) at a rotation speed of 2500 rpm for 4 hours using a bead mill apparatus (manufactured by AIMEX CO., Ltd.: RMB Batch-Type Ready Mill).

(93) Using a stainless steel material filter (mesh: 0.35 mm) attached to a bead separation container (manufactured by AIMEX CO., Ltd.), the silicon nanoparticles including the beads are subjected to suction filtration to separate the beads from the silicon nanoparticles separated from the beads is heated to 30° C. to 35° C. using a vacuum evaporator, so that the isopropyl alcohol (IPA) solution is evaporated to give the silicon nanoparticles and/or aggregates thereof.

(94) The silicon nanoparticles obtained by the above-mentioned method mainly include, as in the first embodiment, silicon nanoparticles having a crystallite diameter of 1 nm or more and 100 nm or less. Main silicon nanoparticles have a crystallite diameter of about 2 nm or more and 20 nm or less as in the first embodiment.

(95) Specifically, 15 g of a high-purity Si powder is dispersed in 300 ml of a 99% or more isopropyl alcohol (IPA) solution, φ0.5 μm zirconia beads (volume: 300 ml) are added, and the mixture is finely divided by performing grinding (one-step grinding) at a rotation speed of 2500 rpm for 4 hours using a bead mill apparatus (manufactured by AIMEX CO., Ltd.: RMB Batch-Type Ready Mill).

(96) Using a stainless steel material filter (mesh: 0.35 mm) attached to a bead separation container (manufactured by AIMEX CO., Ltd.), the silicon nanoparticles including the beads are subjected to suction filtration to separate the beads from the silicon nanoparticles. The IPA solution containing the silicon nanoparticles separated from the beads is heated to 40° C. using a vacuum evaporator, so that IPA is evaporated to give the silicon nanoparticles and/or aggregates thereof.

(97) As in the first embodiment, the silicon nanoparticles obtained by the above-mentioned method include, as a main component, silicon nanoparticles mainly having a crystallite diameter of 1 nm or more and 100 nm or less. Main silicon nanoparticles have a crystallite diameter of about 2 nm or more and 20 nm or less as in the first embodiment.

(98) In the same manner as in the first embodiment, the first mixing step of mixing hydrogen peroxide water with the silicon nanoparticles in a glass container is performed thereafter also in the present embodiment. The treatment of the surfaces of the silicon nanoparticles with hydrogen peroxide water is capable of forming silicon nanoparticles having a relatively thin and heterogeneous/incomplete oxide film on the surfaces thereof. As a result, the silicon nanoparticles (and silicon fine particles including, as main particles, the silicon nanoparticles) and/or aggregates thereof are capable of forming a state in which they have surfaces capable of getting direct contact with a medium capable of containing a water-containing liquid, while as a whole retaining hydrophilicity on their surfaces. Such a special surface treatment is capable of promoting the generation of hydrogen with higher accuracy.

(99) Thereafter, the silicon nanoparticles possibly having the isopropyl alcohol (IPA) solution partially attached thereto are subjected to a solid-liquid separation treatment using a known centrifugal separator to remove the isopropyl alcohol (IPA) solution with high accuracy and then sufficiently dried to produce one type of final silicon nanoparticles according to the present embodiment.

(100) In the present embodiment, as another type of final silicon nanoparticles, silicon nanoparticles were also produced, with the mixing time of the hydrogen peroxide water with the silicon nanoparticles set to 60 minutes in the first mixing step of the above-described steps.

(101) The silicon nanoparticles can be, in the same manner as in the first embodiment, mixed with a sodium hydrogencarbonate powder to give a mixture, which is kneaded and then subjected to a tableting method to give a solid formulation.

(102) Thereafter, the amount of hydrogen generated by contact between the silicon nanoparticles and the medium was examined to give the same results as the results of the first embodiment shown in FIG. 4.

Other Embodiments

(103) One aspect of the production method for silicon fine particles in the compound includes a step of finely dividing silicon particles having a crystal grain diameter of more than 1 μm by a physical grinding method to form silicon fine particles mainly having a crystallite diameter of 1 nm or more and 100 nm or less. A suitable example of the physical grinding method is a method of grinding silicon particles by a beam mill grinding method, a planetary ball mill grinding method, a jet mill grinding method, or a combination of two or more thereof. However, in terms of production costs or ease of production control, a particularly suitable example is only a bead mill grinding method or a grinding method including at least a bead mill grinding method. The exemplified solid formulations (compounds) in the embodiments not only play a role as the hydrogen supply material but also play a role as a hydrogen generation material for a living body that enables safe generation of hydrogen in vivo or ex vivo (hydrogen supply material for a living body).

(104) The embodiments employ, as a starting material, silicon particles i.e. a commercially available high-purity silicon particle powder. The starting material, however, is not limited to such silicon particles. One preferred aspect is also employing, as the starting material, for example, silicon chips, silicon cutting scraps, or silicon polishing scraps (hereinafter, also referred to as “silicon chips etc.” or “chips etc.”) which are usually disposed of as wastes in cutting processing of silicon in a process for production of a silicon wafer to be used in semiconductor products such as a solar cell, in terms of attaining lower cost and/or giving finer silicon nanoparticles. The object of the “silicon fine particles” is not limited to crystalline silicon. For example, it is also possible to use, as the starting material in the embodiments, silicon particles obtained by finely dividing an amorphous silicon layer formed on a known substrate by a CVD method. It is also possible to use, as the starting material or the finally-formed silicon fine particles in the embodiments, amorphous or crystalline silicon particles somewhat directly produced by, for example, a CVD method, a laser method, or an arc-discharge method.

(105) The disclosure of the embodiments or the examples is intended for describing the embodiments and is not intended for limiting the present invention. In addition, modified examples within the scope of the present invention, including other combinations of the embodiments and the examples, are also to be included in the scope of claims.

INDUSTRIAL APPLICABILITY

(106) A compound and a hydrogen supply method according to the present invention can be widely use din agriculture, agriculture and stock raising forestry, fishery, a pet industry, industries of bonsai plants and flower arrangement, or medical industries including a veterinary industry and a tree doctor industry.