WO2020122042A1 - Method for producing mixture containing liquid, gas, or solid with regulated fine particle diameter - Google Patents
Method for producing mixture containing liquid, gas, or solid with regulated fine particle diameter Download PDFInfo
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- WO2020122042A1 WO2020122042A1 PCT/JP2019/048195 JP2019048195W WO2020122042A1 WO 2020122042 A1 WO2020122042 A1 WO 2020122042A1 JP 2019048195 W JP2019048195 W JP 2019048195W WO 2020122042 A1 WO2020122042 A1 WO 2020122042A1
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- 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
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
- A61K8/04—Dispersions; Emulsions
- A61K8/06—Emulsions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/92—Oils, fats or waxes; Derivatives thereof, e.g. hydrogenation products thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
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- 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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/60—Salad dressings; Mayonnaise; Ketchup
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- the present invention relates to a method for producing a mixture containing a liquid, a gas or a solid having an adjusted fine particle size.
- the present invention solves the above problems and provides a method for producing a liquid-solid-gas mixture having fine particle diameters, which has the following inventive constitution.
- Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size.
- the first step, Incompatible liquid A and liquid B are mixed and pulverized by a second liquid atomization device to obtain a second mixture emulsion (A′ ⁇ B emulsion) containing A′ particles of different fine particle diameters.
- the two steps, the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (A′ ⁇ B emulsion) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture emulsion (A ⁇ A′ ⁇ B emulsion).
- Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size.
- the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (B/C emulsion) obtained in the second step are mixed at a constant ratio to obtain a third mixture emulsion.
- Liquid B and gas X are mixed and pulverized by a first gas/liquid atomization device, and a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter (B ⁇ ).
- the first step of acquiring (X gas/liquid mixture) Liquid B and gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B containing a gas/liquid mixture containing X′ gas particles having a particle size of another minute size (B
- a second step of obtaining (X' gas-liquid mixture) The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X′ gas/liquid mixture) obtained in the second step
- a third step of producing a third adjusted mixture (B/X/X' gas/liquid mixture) by mixing at a fixed ratio, and manufacturing a regulated micro-sized gas/liquid mixture.
- the liquid B and the gas X are mixed and pulverized by the first gas/liquid refiner to be a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter).
- the first step of acquiring (X gas/liquid mixture) The liquid B and the gas Y are mixed and pulverized by a second gas/liquid refiner, and a second gas/liquid mixture (B/Y gas) is formed from a gas/liquid mixture containing Y gas particles having a constant fine particle diameter.
- a second step of obtaining a liquid mixture The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. And a third step of producing a third adjusted mixture (B/X/Y gas/liquid mixture) by mixing in proportions.
- Incompatible liquid A and liquid B are mixed and pulverized by the first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing liquid particles of A having a certain fine particle size.
- the first step to do, Liquid B and solid Z are mixed and pulverized by a second solid/liquid refining device to form a second solid/liquid mixture (B.
- a second step of obtaining a Z solid/liquid mixture) The first liquid mixture (A/B liquid mixture) obtained in the first step and the second solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step are mixed at a constant ratio.
- Liquid B and solid Z are mixed and crushed by a first solid/liquid refining device to form a first solid/liquid mixture (B ⁇ The first step of obtaining a Z solid/liquid mixture), The liquid B and the gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B.
- a second step of obtaining (X gas/liquid mixture) The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant.
- a third step of producing a third adjusted mixture (B/X/Z gas/solid/liquid mixture) by mixing in a ratio, and a controlled micro-sized gas/solid/liquid mixture. Manufacturing method.
- Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size.
- the first step, Liquid B and solid Z are mixed and pulverized by a solid/liquid refining device to obtain a solid/liquid mixture (B/Z solid/liquid mixture) consisting of a solid/liquid mixture containing Z solid particles having a constant fine particle size.
- the second step is to mix the liquid B and the gas X with a gas/liquid refiner and pulverize them to form a gas/liquid mixture (B.
- X gas-liquid mixture third step, The first mixture emulsion (A/B emulsion) obtained in the first step, the solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step, and the gas/gas mixture obtained in the third step And a fourth step of producing a third adjusted mixture (A/B/X/Z gas/solid/liquid mixture) by mixing the liquid mixture (B/X gas/liquid mixture) at a constant ratio.
- a method for producing a regulated micro-sized gas-solid-liquid mixture which is characterized in that [8] Any one of [1], [2], [5] or [7], characterized in that the liquid A is a water-insoluble liquid fuel such as heavy oil and kerosene, and the liquid B is water.
- the liquid A is edible oil such as sesame oil, rice oil, and salad oil
- the liquid B is water [1], [2], [5] or [7].
- the liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil, squalane, etc.
- the liquid B is water [1], [2], [5] or [7].
- the method for producing the adjusted microsized mixture according to any one of 1. [11] The adjustment according to any one of [3], [4], [6] or [7], wherein the gas X is air, nitrogen or hydrogen and the liquid B is water.
- a method for producing a micro-sized gas-liquid mixture [12] The adjusted minute amount according to any one of [3], [4], [6] or [7], wherein the gas Y is oxygen or ozone and the liquid B is water. Manufacturing method of size gas-liquid mixture. [13] The atmosphere described in any one of [3], [4], [6], [7], [8], [9], [11] or [12].
- a method for producing a micro-sized gas-liquid mixture, wherein the liquid mixture is microbubble water or nanobubble water.
- the present invention it is possible to easily provide a mixture of various fine particle sizes of liquid, solid, and gas in a state in which the particle size is controlled, and it is possible to use it for various applications and to exert its effects.
- water H 2 O becomes H + and O ⁇ by being ionized
- carbon (C) which is the main component of the oily fuel, bonds with oxygen (O) to become CO 2.
- O oxygen
- it binds to these ions to form CH and COH, and eventually suppresses the generation of CO 2 .
- the liquid A include heavy oil or kerosene as an oily fuel, salad oil as an edible oil, rice oil, sesame oil, and the like
- the liquid B includes water, which is an emulsion as a fine mixture y thereof.
- emulsion manufacturing device another liquid refining device (emulsion manufacturing device), and the different emulsions are mixed at a constant ratio to manufacture a mixture emulsion (A/A'/B emulsion) having a controlled particle size.
- A/A'/B emulsion a mixture emulsion having a controlled particle size.
- the produced emulsion is commercialized as a hydrofuel, an edible dressing, or the like.
- water B and a gas for example, air X
- a gas/liquid micronization device for example, water B and a gas, for example, air X
- a gas containing gas particles having a constant fine particle diameter is formed.
- a second gas/liquid mixture (B/X′ gas/liquid mixture) consisting of a gas/liquid mixture containing air X′ gas particles having a particle size of
- the liquid mixture (B/X gas/liquid mixture) and the second gas/liquid mixture (water/air X, air X′ gas/liquid mixture) obtained in the second step are mixed at a constant ratio to form a third mixture.
- a conditioned mixture water B/air X/air X′ gas/liquid mixture.
- the liquid (water) B and the gas X (air) are mixed and pulverized by the first gas/liquid atomization device to form a first gas composed of a gas/liquid mixture containing X gas particles having a constant fine particle diameter.
- a first step of obtaining a liquid mixture (B water/X air, gas/liquid mixture), Liquid B water and gaseous Y hydrogen are mixed and pulverized by a second gas/liquid atomizing device to form a second gas/liquid mixture (B) containing a gas/liquid mixture containing Y hydrogen gas particles having a constant fine particle diameter.
- a second step of obtaining a water/Y hydrogen gas/liquid mixture) The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. It is possible to mix in proportions to produce a third conditioned mixture (B water/X air/Y hydrogen:gas/liquid mixture).
- liquid B water
- solid Z coal
- the liquid B and the gas X (air) are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (nano bubble water) containing X gas particles of a certain fine size is formed.
- a second step of obtaining a gas/liquid mixture (B/X gas/liquid mixture (nanobubble water));
- the first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant.
- B water).X (air).Z (coal): gas-solid-liquid mixture).
- the mixture is burned as a good fuel in a boiler to generate energy.
- the liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil and squalane
- the liquid B is water.
- the gas X may be air, nitrogen or hydrogen
- the liquid B may be water
- the gas Y may be oxygen or ozone.
- FIG. 1 is a flow chart of an embodiment of the present invention.
- the first liquid atomization apparatus 1 water and oil (kerosene) are mixed to generate an emulsion having a constant particle size, while the second body is used.
- the refining device 2 water and oil (heavy oil) are mixed to generate an emulsion having a constant particle size.
- water and air are mixed in the gas-liquid refiner 3 to generate nanobubble water.
- the emulsion produced by the first liquid atomizing device 1, the emulsion produced by the second body atomizing device 2 and the nanobubble water produced by the gas-liquid atomizing device 3 are put into a mixer 4.
- the mixed hydrofuel produced in this way is supplied to an inland engine (engine) or a boiler for combustion to improve combustion efficiency and complete combustion to discharge purified gas, thereby avoiding environmental pollution.
- First liquid refining device 2 Second body refining device 3: Gas-liquid refining device 4: Mixer
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Abstract
[Problem] To easily provide a mixture of a liquid, a solid, and a gas which have various regulated fine particle diameters. [Solution] A production method comprising: a first step, in which liquid A and liquid B which are incompatible are mixed together and pulverized by a first liquid pulverizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a certain fine particle diameter; a second step, in which liquid B and solid Z are mixed together and pulverized by a solid/liquid pulverizer to obtain a solid/liquid mixture (B/Z solid/liquid mixture) containing solid Z particles having a certain fine particle diameter; a third step, in which liquid B and gas X are mixed together and pulverized by a gas/liquid pulverizer to obtain a gas/liquid mixture (B/X gas/liquid mixture) containing gas X particles having a certain fine particle diameter; and a fourth step, in which the mixtures obtained in the above steps are mixed together. For example, the liquid A may be a liquid fuel such as a heavy oil or kerosene, the gas X may be air, nitrogen, or hydrogen, and the solid Z may be coal, a cereal, silver, or gold.
Description
本願発明は、調整された微小粒子径の液体、気体又は固体を含有する混合物の製造方法に関するものである。
The present invention relates to a method for producing a mixture containing a liquid, a gas or a solid having an adjusted fine particle size.
従来、内燃機関用の液体燃料に水を混ぜてエマルジョンとした燃料が開発され、ある程度の燃費向上の効果が得られている。また、マイクロバブル水、ナノバブル水等の微細気泡を含有した水を汚水処理や健康増進剤として使用することが行われている。
しかしながら、それらの各種材料の粒子径を制御して使用する技術は提案されていない。 BACKGROUND ART Conventionally, a fuel which has been made into an emulsion by mixing water with a liquid fuel for an internal combustion engine has been developed, and an effect of improving fuel efficiency to some extent has been obtained. In addition, water containing fine bubbles such as micro-bubble water and nano-bubble water is used as a sewage treatment and a health promoting agent.
However, no technique has been proposed for controlling the particle size of these various materials for use.
しかしながら、それらの各種材料の粒子径を制御して使用する技術は提案されていない。 BACKGROUND ART Conventionally, a fuel which has been made into an emulsion by mixing water with a liquid fuel for an internal combustion engine has been developed, and an effect of improving fuel efficiency to some extent has been obtained. In addition, water containing fine bubbles such as micro-bubble water and nano-bubble water is used as a sewage treatment and a health promoting agent.
However, no technique has been proposed for controlling the particle size of these various materials for use.
しかしながら、それらの各種材料の微細粒子径を制御して使用する技術は提案されていない。
However, no technology has been proposed for controlling and using the fine particle diameter of these various materials.
本願発明は上記課題を解決するものであって、下記発明構成の微小粒子径の液・固・気混合物の製造方法である。
[１] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ａと液体Ｂを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＡ’粒子を含む第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）を取得する第２工程と、第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ａ’・Ｂエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。
[２] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ｂと液体Ｃを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＣ粒子を含む第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）を取得する第２工程と、第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ｂ・Ｃエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。 The present invention solves the above problems and provides a method for producing a liquid-solid-gas mixture having fine particle diameters, which has the following inventive constitution.
[1] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Incompatible liquid A and liquid B are mixed and pulverized by a second liquid atomization device to obtain a second mixture emulsion (A′·B emulsion) containing A′ particles of different fine particle diameters. The two steps, the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (A′·B emulsion) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture emulsion (A·A′·B emulsion).
[2] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Second step of mixing and pulverizing incompatible liquid B and liquid C with a second liquid atomizer to obtain a second mixture emulsion (B/C emulsion) containing C particles of different fine particle sizes And the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (B/C emulsion) obtained in the second step are mixed at a constant ratio to obtain a third mixture emulsion. A third step of producing an adjusted mixture emulsion (A, B, C emulsion), the method for producing an adjusted microsized mixture emulsion.
[１] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ａと液体Ｂを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＡ’粒子を含む第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）を取得する第２工程と、第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ａ’・Ｂエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。
[２] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ｂと液体Ｃを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＣ粒子を含む第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）を取得する第２工程と、第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ｂ・Ｃエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。 The present invention solves the above problems and provides a method for producing a liquid-solid-gas mixture having fine particle diameters, which has the following inventive constitution.
[1] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Incompatible liquid A and liquid B are mixed and pulverized by a second liquid atomization device to obtain a second mixture emulsion (A′·B emulsion) containing A′ particles of different fine particle diameters. The two steps, the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (A′·B emulsion) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture emulsion (A·A′·B emulsion).
[2] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Second step of mixing and pulverizing incompatible liquid B and liquid C with a second liquid atomizer to obtain a second mixture emulsion (B/C emulsion) containing C particles of different fine particle sizes And the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (B/C emulsion) obtained in the second step are mixed at a constant ratio to obtain a third mixture emulsion. A third step of producing an adjusted mixture emulsion (A, B, C emulsion), the method for producing an adjusted microsized mixture emulsion.
[３] 液体Ｂと気体Ｘを第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、別微小サイズの粒子径のＸ’気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ’気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ’気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｘ’気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。
[４] 液体Ｂと気体Ｘを第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第１工程と、
液体Ｂと気体Ｙを第２の気・液微細化装置で混合・粉砕して、一定微小粒子径のＹ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｙ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｙ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｙ気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。 [3] Liquid B and gas X are mixed and pulverized by a first gas/liquid atomization device, and a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter (B・The first step of acquiring (X gas/liquid mixture),
Liquid B and gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B containing a gas/liquid mixture containing X′ gas particles having a particle size of another minute size (B A second step of obtaining (X' gas-liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X′ gas/liquid mixture) obtained in the second step A third step of producing a third adjusted mixture (B/X/X' gas/liquid mixture) by mixing at a fixed ratio, and manufacturing a regulated micro-sized gas/liquid mixture. Method.
[4] The liquid B and the gas X are mixed and pulverized by the first gas/liquid refiner to be a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter).・The first step of acquiring (X gas/liquid mixture),
The liquid B and the gas Y are mixed and pulverized by a second gas/liquid refiner, and a second gas/liquid mixture (B/Y gas) is formed from a gas/liquid mixture containing Y gas particles having a constant fine particle diameter. A second step of obtaining a liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. And a third step of producing a third adjusted mixture (B/X/Y gas/liquid mixture) by mixing in proportions.
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、別微小サイズの粒子径のＸ’気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ’気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ’気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｘ’気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。
[４] 液体Ｂと気体Ｘを第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第１工程と、
液体Ｂと気体Ｙを第２の気・液微細化装置で混合・粉砕して、一定微小粒子径のＹ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｙ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｙ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｙ気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。 [3] Liquid B and gas X are mixed and pulverized by a first gas/liquid atomization device, and a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter (B・The first step of acquiring (X gas/liquid mixture),
Liquid B and gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B containing a gas/liquid mixture containing X′ gas particles having a particle size of another minute size (B A second step of obtaining (X' gas-liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X′ gas/liquid mixture) obtained in the second step A third step of producing a third adjusted mixture (B/X/X' gas/liquid mixture) by mixing at a fixed ratio, and manufacturing a regulated micro-sized gas/liquid mixture. Method.
[4] The liquid B and the gas X are mixed and pulverized by the first gas/liquid refiner to be a first gas/liquid mixture (B containing a gas/liquid mixture containing X gas particles having a constant fine particle diameter).・The first step of acquiring (X gas/liquid mixture),
The liquid B and the gas Y are mixed and pulverized by a second gas/liquid refiner, and a second gas/liquid mixture (B/Y gas) is formed from a gas/liquid mixture containing Y gas particles having a constant fine particle diameter. A second step of obtaining a liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. And a third step of producing a third adjusted mixture (B/X/Y gas/liquid mixture) by mixing in proportions.
[５] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ液体粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
液体Ｂと固体Ｚを第２の固・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＺ固体粒子を含む固・液混合物からなる第２の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、
第１工程で得られた第１の液体混合物（Ａ・Ｂ液体混合物）と第２工程で得られた第２の固・液混合物（Ｂ・Ｚ固・液混合物）とを一定割合で混合して第３の調整された混合物（Ａ・Ｂ・Ｚ固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。
[６] 液体Ｂと固体Ｚを第１の固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる第１の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の固・液混合物（Ｂ・Ｚ固・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。 [5] Incompatible liquid A and liquid B are mixed and pulverized by the first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing liquid particles of A having a certain fine particle size. The first step to do,
Liquid B and solid Z are mixed and pulverized by a second solid/liquid refining device to form a second solid/liquid mixture (B. A second step of obtaining a Z solid/liquid mixture),
The first liquid mixture (A/B liquid mixture) obtained in the first step and the second solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture (A/B/Z solid/liquid mixture).
[6] Liquid B and solid Z are mixed and crushed by a first solid/liquid refining device to form a first solid/liquid mixture (B・The first step of obtaining a Z solid/liquid mixture),
The liquid B and the gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B. A second step of obtaining (X gas/liquid mixture),
The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant. A third step of producing a third adjusted mixture (B/X/Z gas/solid/liquid mixture) by mixing in a ratio, and a controlled micro-sized gas/solid/liquid mixture. Manufacturing method.
液体Ｂと固体Ｚを第２の固・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＺ固体粒子を含む固・液混合物からなる第２の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、
第１工程で得られた第１の液体混合物（Ａ・Ｂ液体混合物）と第２工程で得られた第２の固・液混合物（Ｂ・Ｚ固・液混合物）とを一定割合で混合して第３の調整された混合物（Ａ・Ｂ・Ｚ固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。
[６] 液体Ｂと固体Ｚを第１の固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる第１の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の固・液混合物（Ｂ・Ｚ固・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。 [5] Incompatible liquid A and liquid B are mixed and pulverized by the first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing liquid particles of A having a certain fine particle size. The first step to do,
Liquid B and solid Z are mixed and pulverized by a second solid/liquid refining device to form a second solid/liquid mixture (B. A second step of obtaining a Z solid/liquid mixture),
The first liquid mixture (A/B liquid mixture) obtained in the first step and the second solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture (A/B/Z solid/liquid mixture).
[6] Liquid B and solid Z are mixed and crushed by a first solid/liquid refining device to form a first solid/liquid mixture (B・The first step of obtaining a Z solid/liquid mixture),
The liquid B and the gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B. A second step of obtaining (X gas/liquid mixture),
The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant. A third step of producing a third adjusted mixture (B/X/Z gas/solid/liquid mixture) by mixing in a ratio, and a controlled micro-sized gas/solid/liquid mixture. Manufacturing method.
[７] 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
液体Ｂと固体Ｚを固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、 液体Ｂと気体Ｘを気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第３工程と、
第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と、第２工程で得られた固・液混合物（Ｂ・Ｚ固・液混合物）と第３工程で得られた気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ａ・Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第４工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。
[８] 液体Ａが重油、灯油等の非水溶性の液体燃料であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[９] 液体Ａが胡麻油、米油、サラダ油等の食用油であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[１０] 液体Ａがホホバオイル、ツバキオイル、オリーブオイル、スクワラン等の化粧品用油であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[１１] 気体Ｘが空気又は窒素あるいは水素であり、液体Ｂが水であることを特徴とする[３]、[４]、[６]又は[７]のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。
[１２] 気体Ｙが酸素又はオゾンであり、液体Ｂが水であることを特徴とする[３]、[４]、[６]又は[７]のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。
[１３] 前記[３]、[４]、[６]，[７]、[８]、[９]、[１０]，[１１]又は[１２]のいずれか１項に記載された気・液混合物がマイクロバブル水又はナノバブル水であることを特徴とする微小サイズ気・液混合物の製造方法。 [7] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Liquid B and solid Z are mixed and pulverized by a solid/liquid refining device to obtain a solid/liquid mixture (B/Z solid/liquid mixture) consisting of a solid/liquid mixture containing Z solid particles having a constant fine particle size. The second step is to mix the liquid B and the gas X with a gas/liquid refiner and pulverize them to form a gas/liquid mixture (B. X gas-liquid mixture) third step,
The first mixture emulsion (A/B emulsion) obtained in the first step, the solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step, and the gas/gas mixture obtained in the third step And a fourth step of producing a third adjusted mixture (A/B/X/Z gas/solid/liquid mixture) by mixing the liquid mixture (B/X gas/liquid mixture) at a constant ratio. A method for producing a regulated micro-sized gas-solid-liquid mixture, which is characterized in that
[8] Any one of [1], [2], [5] or [7], characterized in that the liquid A is a water-insoluble liquid fuel such as heavy oil and kerosene, and the liquid B is water. A method for producing a tuned microsized mixture according to paragraph.
[9] The liquid A is edible oil such as sesame oil, rice oil, and salad oil, and the liquid B is water [1], [2], [5] or [7]. The method for producing a tuned micro-sized mixture according to.
[10] The liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil, squalane, etc., and the liquid B is water [1], [2], [5] or [7]. The method for producing the adjusted microsized mixture according to any one of 1.
[11] The adjustment according to any one of [3], [4], [6] or [7], wherein the gas X is air, nitrogen or hydrogen and the liquid B is water. A method for producing a micro-sized gas-liquid mixture.
[12] The adjusted minute amount according to any one of [3], [4], [6] or [7], wherein the gas Y is oxygen or ozone and the liquid B is water. Manufacturing method of size gas-liquid mixture.
[13] The atmosphere described in any one of [3], [4], [6], [7], [8], [9], [11] or [12]. A method for producing a micro-sized gas-liquid mixture, wherein the liquid mixture is microbubble water or nanobubble water.
液体Ｂと固体Ｚを固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、 液体Ｂと気体Ｘを気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第３工程と、
第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と、第２工程で得られた固・液混合物（Ｂ・Ｚ固・液混合物）と第３工程で得られた気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ａ・Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第４工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。
[８] 液体Ａが重油、灯油等の非水溶性の液体燃料であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[９] 液体Ａが胡麻油、米油、サラダ油等の食用油であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[１０] 液体Ａがホホバオイル、ツバキオイル、オリーブオイル、スクワラン等の化粧品用油であり、液体Ｂが水であることを特徴とする[１]、[２]、[５]又は[７]のいずれか１項に記載の調整された微小サイズの混合物の製造方法。
[１１] 気体Ｘが空気又は窒素あるいは水素であり、液体Ｂが水であることを特徴とする[３]、[４]、[６]又は[７]のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。
[１２] 気体Ｙが酸素又はオゾンであり、液体Ｂが水であることを特徴とする[３]、[４]、[６]又は[７]のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。
[１３] 前記[３]、[４]、[６]，[７]、[８]、[９]、[１０]，[１１]又は[１２]のいずれか１項に記載された気・液混合物がマイクロバブル水又はナノバブル水であることを特徴とする微小サイズ気・液混合物の製造方法。 [7] Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. The first step,
Liquid B and solid Z are mixed and pulverized by a solid/liquid refining device to obtain a solid/liquid mixture (B/Z solid/liquid mixture) consisting of a solid/liquid mixture containing Z solid particles having a constant fine particle size. The second step is to mix the liquid B and the gas X with a gas/liquid refiner and pulverize them to form a gas/liquid mixture (B. X gas-liquid mixture) third step,
The first mixture emulsion (A/B emulsion) obtained in the first step, the solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step, and the gas/gas mixture obtained in the third step And a fourth step of producing a third adjusted mixture (A/B/X/Z gas/solid/liquid mixture) by mixing the liquid mixture (B/X gas/liquid mixture) at a constant ratio. A method for producing a regulated micro-sized gas-solid-liquid mixture, which is characterized in that
[8] Any one of [1], [2], [5] or [7], characterized in that the liquid A is a water-insoluble liquid fuel such as heavy oil and kerosene, and the liquid B is water. A method for producing a tuned microsized mixture according to paragraph.
[9] The liquid A is edible oil such as sesame oil, rice oil, and salad oil, and the liquid B is water [1], [2], [5] or [7]. The method for producing a tuned micro-sized mixture according to.
[10] The liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil, squalane, etc., and the liquid B is water [1], [2], [5] or [7]. The method for producing the adjusted microsized mixture according to any one of 1.
[11] The adjustment according to any one of [3], [4], [6] or [7], wherein the gas X is air, nitrogen or hydrogen and the liquid B is water. A method for producing a micro-sized gas-liquid mixture.
[12] The adjusted minute amount according to any one of [3], [4], [6] or [7], wherein the gas Y is oxygen or ozone and the liquid B is water. Manufacturing method of size gas-liquid mixture.
[13] The atmosphere described in any one of [3], [4], [6], [7], [8], [9], [11] or [12]. A method for producing a micro-sized gas-liquid mixture, wherein the liquid mixture is microbubble water or nanobubble water.
本願発明によれば、液体、固体及び気体の各種微小粒子径の混合物を粒径を制御した状態のものとして容易に提供することができ、各種用途に使用でき、効果が発揮される。
そして、例えばナノバブル水においては、水Ｈ2Ｏはイオン化することでＨ+及びＯ-となり、油性燃料の主成分である炭素（Ｃ）が酸素（Ｏ）と結合して、ＣＯ2 となる前に、これらのイオンと結合し、ＣＨ及びＣＯＨとなり、結果的にＣＯ2の発生を抑制する。そして、燃焼時の有害ガスの発生抑制作用を発揮する。 According to the present invention, it is possible to easily provide a mixture of various fine particle sizes of liquid, solid, and gas in a state in which the particle size is controlled, and it is possible to use it for various applications and to exert its effects.
Then, for example, in nanobubble water, water H 2 O becomes H + and O − by being ionized, and carbon (C), which is the main component of the oily fuel, bonds with oxygen (O) to become CO 2. In addition, it binds to these ions to form CH and COH, and eventually suppresses the generation of CO 2 . And, it exerts an effect of suppressing the generation of harmful gas during combustion.
そして、例えばナノバブル水においては、水Ｈ2Ｏはイオン化することでＨ+及びＯ-となり、油性燃料の主成分である炭素（Ｃ）が酸素（Ｏ）と結合して、ＣＯ2 となる前に、これらのイオンと結合し、ＣＨ及びＣＯＨとなり、結果的にＣＯ2の発生を抑制する。そして、燃焼時の有害ガスの発生抑制作用を発揮する。 According to the present invention, it is possible to easily provide a mixture of various fine particle sizes of liquid, solid, and gas in a state in which the particle size is controlled, and it is possible to use it for various applications and to exert its effects.
Then, for example, in nanobubble water, water H 2 O becomes H + and O − by being ionized, and carbon (C), which is the main component of the oily fuel, bonds with oxygen (O) to become CO 2. In addition, it binds to these ions to form CH and COH, and eventually suppresses the generation of CO 2 . And, it exerts an effect of suppressing the generation of harmful gas during combustion.
本願発明の実施の形態を具体的に説明する。
非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程においては、
例えば液体Ａとして油性燃料の重油又は灯油、食用油としてのサラダオイル、米油、ごま油等、が挙げられ、液体Ｂとして水が挙げられ、それら微細混合ｙ物としてのエマルジョンとなる。
そしてそれらを別別の液体微細化装置（エマルジョン製造装置）で製造し、別々のエマルジョンを一定割合で混合して粒径の調整された混合物エマルジョン（Ａ・Ａ’・Ｂエマルジョン）を製造する。
製造されたエマルジョンは、加水燃料や食用ドレッシング等として製品化される。 Embodiments of the present invention will be specifically described.
A first step of mixing and pulverizing incompatible liquids A and B with a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. In
Examples of the liquid A include heavy oil or kerosene as an oily fuel, salad oil as an edible oil, rice oil, sesame oil, and the like, and the liquid B includes water, which is an emulsion as a fine mixture y thereof.
Then, they are manufactured by another liquid refining device (emulsion manufacturing device), and the different emulsions are mixed at a constant ratio to manufacture a mixture emulsion (A/A'/B emulsion) having a controlled particle size.
The produced emulsion is commercialized as a hydrofuel, an edible dressing, or the like.
非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程においては、
例えば液体Ａとして油性燃料の重油又は灯油、食用油としてのサラダオイル、米油、ごま油等、が挙げられ、液体Ｂとして水が挙げられ、それら微細混合ｙ物としてのエマルジョンとなる。
そしてそれらを別別の液体微細化装置（エマルジョン製造装置）で製造し、別々のエマルジョンを一定割合で混合して粒径の調整された混合物エマルジョン（Ａ・Ａ’・Ｂエマルジョン）を製造する。
製造されたエマルジョンは、加水燃料や食用ドレッシング等として製品化される。 Embodiments of the present invention will be specifically described.
A first step of mixing and pulverizing incompatible liquids A and B with a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. In
Examples of the liquid A include heavy oil or kerosene as an oily fuel, salad oil as an edible oil, rice oil, sesame oil, and the like, and the liquid B includes water, which is an emulsion as a fine mixture y thereof.
Then, they are manufactured by another liquid refining device (emulsion manufacturing device), and the different emulsions are mixed at a constant ratio to manufacture a mixture emulsion (A/A'/B emulsion) having a controlled particle size.
The produced emulsion is commercialized as a hydrofuel, an edible dressing, or the like.
また、例えば、マイクロバブル水、ナノバブル水等を製造するには、水Ｂと気体、例えば空気Ｘを気・液微細化装置で混合・粉砕して、一定微小粒子径の気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得し、また水Ｂと空気Ｘを第２の気・液微細化装置で混合・粉砕して、別微小サイズの粒子径の空気Ｘ’気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ’気・液混合物）を取得し、第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（水・空気Ｘ、空気Ｘ’気・液混合物）とを一定割合で混合して第３の調整された混合物（水Ｂ・空気Ｘ・空気Ｘ’気・液混合物）を製造する。
また、液体（水）Ｂと気体Ｘ（空気）を第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ水・Ｘ空気、気・液混合物）を取得する第１工程と、
液体Ｂ水と気体Ｙ水素を第２の気・液微細化装置で混合・粉砕して、一定微小粒子径のＹ水素気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ水・Ｙ水素気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｙ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ水・Ｘ空気・Ｙ水素：気・液混合物）を製造することできる。 Further, for example, in order to produce micro-bubble water, nano-bubble water, etc., water B and a gas, for example, air X, are mixed and pulverized by a gas/liquid micronization device, and a gas containing gas particles having a constant fine particle diameter is formed. Obtain a first gas/liquid mixture (B/X gas/liquid mixture) consisting of a liquid mixture, and mix and pulverize water B and air X with a second gas/liquid micronization device to obtain a different micro size. A second gas/liquid mixture (B/X′ gas/liquid mixture) consisting of a gas/liquid mixture containing air X′ gas particles having a particle size of The liquid mixture (B/X gas/liquid mixture) and the second gas/liquid mixture (water/air X, air X′ gas/liquid mixture) obtained in the second step are mixed at a constant ratio to form a third mixture. To prepare a conditioned mixture (water B/air X/air X′ gas/liquid mixture).
Further, the liquid (water) B and the gas X (air) are mixed and pulverized by the first gas/liquid atomization device to form a first gas composed of a gas/liquid mixture containing X gas particles having a constant fine particle diameter. A first step of obtaining a liquid mixture (B water/X air, gas/liquid mixture),
Liquid B water and gaseous Y hydrogen are mixed and pulverized by a second gas/liquid atomizing device to form a second gas/liquid mixture (B) containing a gas/liquid mixture containing Y hydrogen gas particles having a constant fine particle diameter. A second step of obtaining a water/Y hydrogen gas/liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. It is possible to mix in proportions to produce a third conditioned mixture (B water/X air/Y hydrogen:gas/liquid mixture).
また、液体（水）Ｂと気体Ｘ（空気）を第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ水・Ｘ空気、気・液混合物）を取得する第１工程と、
液体Ｂ水と気体Ｙ水素を第２の気・液微細化装置で混合・粉砕して、一定微小粒子径のＹ水素気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ水・Ｙ水素気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｙ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ水・Ｘ空気・Ｙ水素：気・液混合物）を製造することできる。 Further, for example, in order to produce micro-bubble water, nano-bubble water, etc., water B and a gas, for example, air X, are mixed and pulverized by a gas/liquid micronization device, and a gas containing gas particles having a constant fine particle diameter is formed. Obtain a first gas/liquid mixture (B/X gas/liquid mixture) consisting of a liquid mixture, and mix and pulverize water B and air X with a second gas/liquid micronization device to obtain a different micro size. A second gas/liquid mixture (B/X′ gas/liquid mixture) consisting of a gas/liquid mixture containing air X′ gas particles having a particle size of The liquid mixture (B/X gas/liquid mixture) and the second gas/liquid mixture (water/air X, air X′ gas/liquid mixture) obtained in the second step are mixed at a constant ratio to form a third mixture. To prepare a conditioned mixture (water B/air X/air X′ gas/liquid mixture).
Further, the liquid (water) B and the gas X (air) are mixed and pulverized by the first gas/liquid atomization device to form a first gas composed of a gas/liquid mixture containing X gas particles having a constant fine particle diameter. A first step of obtaining a liquid mixture (B water/X air, gas/liquid mixture),
Liquid B water and gaseous Y hydrogen are mixed and pulverized by a second gas/liquid atomizing device to form a second gas/liquid mixture (B) containing a gas/liquid mixture containing Y hydrogen gas particles having a constant fine particle diameter. A second step of obtaining a water/Y hydrogen gas/liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. It is possible to mix in proportions to produce a third conditioned mixture (B water/X air/Y hydrogen:gas/liquid mixture).
さらに、液・気・固からなる混合物を製造することもできる。
すなわち、液体Ｂ（水）と固体Ｚ（石炭）を第１の固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体（石炭）粒子を含む固・液混合物からなる第１の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘ（空気）を第２の気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物（ナノバブル水）からなる第２の気・液混合物（Ｂ・Ｘ気・液混合物（ナノバブル水））を取得する第２工程と、
第１工程で得られた第１の固・液混合物（Ｂ・Ｚ固・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ（水）・Ｘ（空気）・Ｚ（石炭）：気・固・液混合物）を製造する。これら混合物を例えば優良な燃料としてボイラーで燃焼してエネルギーとなす。 Further, it is possible to produce a mixture of liquid, gas and solid.
That is, the liquid B (water) and the solid Z (coal) are mixed and pulverized by the first solid/liquid refining device to form a solid/liquid mixture containing Z solid (coal) particles having a constant fine particle diameter. A first step of obtaining a solid/liquid mixture (B/Z solid/liquid mixture) of 1;
The liquid B and the gas X (air) are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (nano bubble water) containing X gas particles of a certain fine size is formed. A second step of obtaining a gas/liquid mixture (B/X gas/liquid mixture (nanobubble water));
The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant. Mix in proportions to produce a third adjusted mixture (B (water).X (air).Z (coal): gas-solid-liquid mixture). For example, the mixture is burned as a good fuel in a boiler to generate energy.
すなわち、液体Ｂ（水）と固体Ｚ（石炭）を第１の固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体（石炭）粒子を含む固・液混合物からなる第１の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘ（空気）を第２の気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物（ナノバブル水）からなる第２の気・液混合物（Ｂ・Ｘ気・液混合物（ナノバブル水））を取得する第２工程と、
第１工程で得られた第１の固・液混合物（Ｂ・Ｚ固・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ（水）・Ｘ（空気）・Ｚ（石炭）：気・固・液混合物）を製造する。これら混合物を例えば優良な燃料としてボイラーで燃焼してエネルギーとなす。 Further, it is possible to produce a mixture of liquid, gas and solid.
That is, the liquid B (water) and the solid Z (coal) are mixed and pulverized by the first solid/liquid refining device to form a solid/liquid mixture containing Z solid (coal) particles having a constant fine particle diameter. A first step of obtaining a solid/liquid mixture (B/Z solid/liquid mixture) of 1;
The liquid B and the gas X (air) are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (nano bubble water) containing X gas particles of a certain fine size is formed. A second step of obtaining a gas/liquid mixture (B/X gas/liquid mixture (nanobubble water));
The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant. Mix in proportions to produce a third adjusted mixture (B (water).X (air).Z (coal): gas-solid-liquid mixture). For example, the mixture is burned as a good fuel in a boiler to generate energy.
上記において、
液体Ａがホホバオイル、ツバキオイル、オリーブオイル、スクワラン等の化粧品用油であり、液体Ｂが水であることも好ましい。
気体Ｘが空気、窒素又は水素であり、液体Ｂが水であること、気体Ｙが酸素又はオゾンであってもよい。 In the above,
It is also preferable that the liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil and squalane, and the liquid B is water.
The gas X may be air, nitrogen or hydrogen, the liquid B may be water, and the gas Y may be oxygen or ozone.
液体Ａがホホバオイル、ツバキオイル、オリーブオイル、スクワラン等の化粧品用油であり、液体Ｂが水であることも好ましい。
気体Ｘが空気、窒素又は水素であり、液体Ｂが水であること、気体Ｙが酸素又はオゾンであってもよい。 In the above,
It is also preferable that the liquid A is a cosmetic oil such as jojoba oil, camellia oil, olive oil and squalane, and the liquid B is water.
The gas X may be air, nitrogen or hydrogen, the liquid B may be water, and the gas Y may be oxygen or ozone.
図１は本願発明の一実施例のフローチャート図であり、第１の液体微細化装置１において、水と油（灯油）を混合して一定粒径サイズのエマルジョンを生成させる一方、第２の体微細化装置２において水と油（重油）を混合して一定粒径サイズのエマルジョンを生成させる。
さらに、気液微細化装置３において水と空気を混合してナノバブル水を生成させる。
次いで、上記第１の液体微細化装置１で生成されたエマルジョンと第２の体微細化装置２で生成されたエマルジョンと気液微細化装置３で生成されたナノバブル水を混合機４に入れて混合する。
こうして製造された混合加水燃料を内南機関（エンジン）やボイラーに供給して燃焼させ、燃焼効率を高め、完全燃焼化させて清浄化ガスを排出させて、環境汚染を回避させる。 FIG. 1 is a flow chart of an embodiment of the present invention. In the first liquid atomization apparatus 1, water and oil (kerosene) are mixed to generate an emulsion having a constant particle size, while the second body is used. In therefining device 2, water and oil (heavy oil) are mixed to generate an emulsion having a constant particle size.
Further, water and air are mixed in the gas-liquid refiner 3 to generate nanobubble water.
Next, the emulsion produced by the first liquid atomizing device 1, the emulsion produced by the secondbody atomizing device 2 and the nanobubble water produced by the gas-liquid atomizing device 3 are put into a mixer 4. Mix.
The mixed hydrofuel produced in this way is supplied to an inland engine (engine) or a boiler for combustion to improve combustion efficiency and complete combustion to discharge purified gas, thereby avoiding environmental pollution.
さらに、気液微細化装置３において水と空気を混合してナノバブル水を生成させる。
次いで、上記第１の液体微細化装置１で生成されたエマルジョンと第２の体微細化装置２で生成されたエマルジョンと気液微細化装置３で生成されたナノバブル水を混合機４に入れて混合する。
こうして製造された混合加水燃料を内南機関（エンジン）やボイラーに供給して燃焼させ、燃焼効率を高め、完全燃焼化させて清浄化ガスを排出させて、環境汚染を回避させる。 FIG. 1 is a flow chart of an embodiment of the present invention. In the first liquid atomization apparatus 1, water and oil (kerosene) are mixed to generate an emulsion having a constant particle size, while the second body is used. In the
Further, water and air are mixed in the gas-
Next, the emulsion produced by the first liquid atomizing device 1, the emulsion produced by the second
The mixed hydrofuel produced in this way is supplied to an inland engine (engine) or a boiler for combustion to improve combustion efficiency and complete combustion to discharge purified gas, thereby avoiding environmental pollution.
１：第１の液体微細化装置
２：第２の体微細化装置
３：気液微細化装置
４：混合機
1: First liquid refining device 2: Second body refining device 3: Gas-liquid refining device 4: Mixer
２：第２の体微細化装置
３：気液微細化装置
４：混合機
1: First liquid refining device 2: Second body refining device 3: Gas-liquid refining device 4: Mixer
Claims (13)
- 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ａと液体Ｂを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＡ’粒子を含む第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）を取得する第２工程と、
第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ａ’・Ｂエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ａ’・Ｂエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。 A first step of mixing and pulverizing incompatible liquids A and B with a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. When,
Incompatible liquid A and liquid B are mixed and pulverized by a second liquid atomization device to obtain a second mixture emulsion (A′·B emulsion) containing A′ particles of different fine particle diameters. 2 steps,
Third mixture by mixing the first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (A′/B emulsion) obtained in the second step at a constant ratio And a third step of producing a mixed emulsion (A·A′·B emulsion) prepared as described above. - 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
非相溶性の液体Ｂと液体Ｃを第２の液体微細化装置で混合・粉砕して、別微小粒子径のＣ粒子を含む第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）を取得する第２工程と、
第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と第２工程で得られた第２の混合物エマルジョン（Ｂ・Ｃエマルジョン）とを一定割合で混合して第３の調整された混合物エマルジョン（Ａ・Ｂ・Ｃエマルジョン）を製造する第３工程とからなることを特徴とする調整された微小サイズの混合物エマルジョンの製造方法。 A first step of mixing and pulverizing incompatible liquids A and B with a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. When,
Second step of mixing and pulverizing incompatible liquid B and liquid C with a second liquid atomizer to obtain a second mixture emulsion (B/C emulsion) containing C particles of different fine particle sizes When,
The first mixture emulsion (A/B emulsion) obtained in the first step and the second mixture emulsion (B/C emulsion) obtained in the second step are mixed at a constant ratio to make a third adjustment. And a third step for producing a mixed emulsion (A, B, C emulsion). - 液体Ｂと気体Ｘを第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、別微小サイズの粒子径のＸ’気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ’気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ’気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｘ’気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。 The liquid B and the gas X are mixed and pulverized by the first gas/liquid atomization device, and the first gas/liquid mixture (B/X gas) is formed from a gas/liquid mixture containing X gas particles having a constant fine particle diameter. A first step of obtaining a liquid mixture),
Liquid B and gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B containing a gas/liquid mixture containing X′ gas particles having a particle size of another minute size (B A second step of obtaining (X' gas-liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X′ gas/liquid mixture) obtained in the second step A third step of producing a third adjusted mixture (B/X/X' gas/liquid mixture) by mixing at a fixed ratio, and manufacturing a regulated micro-sized gas/liquid mixture. Method. - 液体Ｂと気体Ｘを第１の気・液微細化装置で混合・粉砕して、一定微小粒子径のＸ気体粒子を含む気・液混合物からなる第１の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第１工程と、
液体Ｂと気体Ｙを第２の気・液微細化装置で混合・粉砕して、一定微小粒子径のＹ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｙ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の気・液混合物（Ｂ・Ｘ気・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｙ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｙ気・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・液混合物の製造方法。 The liquid B and the gas X are mixed and pulverized by the first gas/liquid atomization device, and the first gas/liquid mixture (B/X gas) is formed from a gas/liquid mixture containing X gas particles having a constant fine particle diameter. A first step of obtaining a liquid mixture),
The liquid B and the gas Y are mixed and pulverized by a second gas/liquid refiner, and a second gas/liquid mixture (B/Y gas) is formed from a gas/liquid mixture containing Y gas particles having a constant fine particle diameter. A second step of obtaining a liquid mixture),
The first gas/liquid mixture (B/X gas/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/Y gas/liquid mixture) obtained in the second step are kept constant. And a third step of producing a third adjusted mixture (B/X/Y gas/liquid mixture) by mixing in proportions. - 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ液体粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
液体Ｂと固体Ｚを第２の固・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＺ固体粒子を含む固・液混合物からなる第２の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、
第１工程で得られた第１の液体混合物（Ａ・Ｂ液体混合物）と第２工程で得られた第２の固・液混合物（Ｂ・Ｚ固・液混合物）とを一定割合で混合して第３の調整された混合物（Ａ・Ｂ・Ｚ固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。 Incompatible liquid A and liquid B are mixed and pulverized by a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A liquid particles having a constant fine particle diameter. Process,
Liquid B and solid Z are mixed and pulverized by a second solid/liquid refining device to form a second solid/liquid mixture (B. A second step of obtaining a Z solid/liquid mixture),
The first liquid mixture (A/B liquid mixture) obtained in the first step and the second solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step are mixed at a constant ratio. And a third step of producing a third adjusted mixture (A/B/Z solid/liquid mixture). - 液体Ｂと固体Ｚを第１の固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる第１の固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第１工程と、
液体Ｂと気体Ｘを第２の気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる第２の気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第２工程と、
第１工程で得られた第１の固・液混合物（Ｂ・Ｚ固・液混合物）と第２工程で得られた第２の気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第３の調整された混合物（Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第３工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。 The liquid B and the solid Z are mixed and crushed by the first solid/liquid refining device to form a first solid/liquid mixture (B/Z solid) including a solid/liquid mixture containing Z solid particles having a constant fine particle diameter. A first step of obtaining a liquid mixture),
The liquid B and the gas X are mixed and pulverized by a second gas/liquid atomization device, and a second gas/liquid mixture (B. A second step of obtaining (X gas/liquid mixture),
The first solid/liquid mixture (B/Z solid/liquid mixture) obtained in the first step and the second gas/liquid mixture (B/X gas/liquid mixture) obtained in the second step are kept constant. A third step of producing a third adjusted mixture (B/X/Z gas/solid/liquid mixture) by mixing in a ratio, and a controlled micro-sized gas/solid/liquid mixture. Manufacturing method. - 非相溶性の液体Ａと液体Ｂを第１の液体微細化装置で混合・粉砕して、一定微小粒子径のＡ粒子を含む第１の混合物エマルジョン（Ａ・Ｂエマルジョン）を取得する第１工程と、
液体Ｂと固体Ｚを固・液微細化装置で混合・粉砕して、一定微小粒子径のＺ固体粒子を含む固・液混合物からなる固・液混合物（Ｂ・Ｚ固・液混合物）を取得する第２工程と、
液体Ｂと気体Ｘを気・液微細化装置で混合・粉砕して、一定微小サイズの粒子径のＸ気体粒子を含む気・液混合物からなる気・液混合物（Ｂ・Ｘ気・液混合物）を取得する第３
工程と、
第１工程で得られた第１の混合物エマルジョン（Ａ・Ｂエマルジョン）と、第２工程で得られた固・液混合物（Ｂ・Ｚ固・液混合物）と第３工程で得られた気・液混合物（Ｂ・Ｘ気・液混合物）とを一定割合で混合して第４の調整された混合物（Ａ・Ｂ・Ｘ・Ｚ気・固・液混合物）を製造する第４工程とからなることを特徴とする調整された微小サイズ気・固・液混合物の製造方法。 A first step of mixing and pulverizing incompatible liquids A and B with a first liquid atomizer to obtain a first mixture emulsion (A/B emulsion) containing A particles having a constant fine particle size. When,
Liquid B and solid Z are mixed and pulverized by a solid/liquid refining device to obtain a solid/liquid mixture (B/Z solid/liquid mixture) consisting of a solid/liquid mixture containing Z solid particles having a constant fine particle size. A second step of
Liquid-B and gas X are mixed and pulverized by a gas-liquid refiner, and a gas-liquid mixture (B-X gas-liquid mixture) is formed from a gas-liquid mixture containing X gas particles having a certain fine size. Third to get
Process,
The first mixture emulsion (A/B emulsion) obtained in the first step, the solid/liquid mixture (B/Z solid/liquid mixture) obtained in the second step, and the gas/gas mixture obtained in the third step A fourth step of producing a fourth adjusted mixture (A/B/X/Z gas/solid/liquid mixture) by mixing the liquid mixture (B/X gas/liquid mixture) at a constant ratio. A method for producing a regulated micro-sized gas-solid-liquid mixture, which is characterized in that - 液体Ａが重油、灯油等の非水溶性の液体燃料であり、液体Ｂが水であることを特徴とする請求項１、２、５又は７のいずれか１項に記載の調整された微小サイズの混合物の製造方法。 Liquid A is a water-insoluble liquid fuel such as heavy oil or kerosene, and liquid B is water. Adjusted minute size according to any one of claims 1, 2, 5 or 7. A method for producing a mixture.
- 液体Ａが胡麻油、米油、サラダ油等の食用油であり、液体Ｂが水であることを特徴とする請求項１、２、５又は７のいずれか１項に記載の調整された微小サイズの混合物の製造方法。 Liquid A is edible oil such as sesame oil, rice oil, salad oil and the like, and liquid B is water. The adjusted fine size according to any one of claims 1, 2, 5 and 7. A method for producing a mixture.
- 液体Ａがホホバオイル、ツバキオイル、オリーブオイル、スクワラン等の化粧品用油であり、液体Ｂが水であることを特徴とする請求項１、２、５又は７のいずれか１項に記載の調整された微小サイズの混合物の製造方法。 Liquid A is cosmetic oil such as jojoba oil, camellia oil, olive oil, squalane, etc., and liquid B is water, The adjustment according to any one of claims 1, 2, 5 or 7. For producing a micro-sized mixture as described above.
- 気体Ｘが空気又は窒素あるいは水素であり、液体Ｂが水であることを特徴とする請求項３、４、６又は７のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。 8. Preparation of a regulated microsized gas-liquid mixture according to any one of claims 3, 4, 6 or 7, characterized in that the gas X is air or nitrogen or hydrogen and the liquid B is water. Method.
- 気体Ｙが酸素又はオゾンであり、液体Ｂが水であることを特徴とする請求項３、４、６又は７のいずれか１項に記載の調整された微小サイズ気・液混合物の製造方法。 The method for producing the adjusted micro-sized gas-liquid mixture according to any one of claims 3, 4, 6 and 7, wherein the gas Y is oxygen or ozone and the liquid B is water.
- 請求項３、４、６，７、８、９、１０，１１又は１２のいずれか１項に記載された気・液混合物がマイクロバブル水又はナノバブル水であることを特徴とする微小サイズ気・液混合物の製造方法。
A micro-sized gas characterized in that the gas-liquid mixture according to any one of claims 3, 4, 6, 7, 8, 9, 10, 11 or 12 is microbubble water or nanobubble water. A method for producing a liquid mixture.
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Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63150221A (en) * | 1986-12-15 | 1988-06-22 | Shiseido Co Ltd | Emulsified composition containing crystalline drug |
| JPH02174927A (en) * | 1988-12-27 | 1990-07-06 | Pola Chem Ind Inc | O/w type multiphase emulsion and preparation thereof |
| JPH06145676A (en) * | 1992-11-04 | 1994-05-27 | Kao Corp | Heavy oil-mixed fuel |
| JP2004027223A (en) * | 2002-06-03 | 2004-01-29 | Intevep Sa | Manufacturing method of stable emulsion using dynamic mixer or static mixer |
| JP2005139189A (en) * | 2003-11-07 | 2005-06-02 | L'oreal Sa | Emulsion-containing makeup composition |
| US20080148626A1 (en) * | 2006-12-20 | 2008-06-26 | Diamond Qc Technologies Inc. | Multiple polydispersed fuel emulsion |
| JP2012017262A (en) * | 2010-07-06 | 2012-01-26 | Kao Corp | Method for producing cosmetic |
| JP2012052094A (en) * | 2010-08-06 | 2012-03-15 | Opt Creation:Kk | Nano bubble fuel and combustion system |
| JP2013141664A (en) * | 2012-01-12 | 2013-07-22 | San Nopco Ltd | Antifoaming agent |
| JP2014055304A (en) * | 2006-12-18 | 2014-03-27 | Diamond Qc Technologies Inc | Polydispersed mixed emulsion |
| JP2017052739A (en) * | 2015-09-11 | 2017-03-16 | 株式会社熊本アイディーエム | Transfusion solution generator and transfusion solution production method, and transfusion solution |
-
2018
- 2018-12-11 JP JP2018231809A patent/JP2020093200A/en active Pending
-
2019
- 2019-12-10 WO PCT/JP2019/048195 patent/WO2020122042A1/en active Application Filing
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63150221A (en) * | 1986-12-15 | 1988-06-22 | Shiseido Co Ltd | Emulsified composition containing crystalline drug |
| JPH02174927A (en) * | 1988-12-27 | 1990-07-06 | Pola Chem Ind Inc | O/w type multiphase emulsion and preparation thereof |
| JPH06145676A (en) * | 1992-11-04 | 1994-05-27 | Kao Corp | Heavy oil-mixed fuel |
| JP2004027223A (en) * | 2002-06-03 | 2004-01-29 | Intevep Sa | Manufacturing method of stable emulsion using dynamic mixer or static mixer |
| JP2005139189A (en) * | 2003-11-07 | 2005-06-02 | L'oreal Sa | Emulsion-containing makeup composition |
| JP2014055304A (en) * | 2006-12-18 | 2014-03-27 | Diamond Qc Technologies Inc | Polydispersed mixed emulsion |
| US20080148626A1 (en) * | 2006-12-20 | 2008-06-26 | Diamond Qc Technologies Inc. | Multiple polydispersed fuel emulsion |
| JP2012017262A (en) * | 2010-07-06 | 2012-01-26 | Kao Corp | Method for producing cosmetic |
| JP2012052094A (en) * | 2010-08-06 | 2012-03-15 | Opt Creation:Kk | Nano bubble fuel and combustion system |
| JP2013141664A (en) * | 2012-01-12 | 2013-07-22 | San Nopco Ltd | Antifoaming agent |
| JP2017052739A (en) * | 2015-09-11 | 2017-03-16 | 株式会社熊本アイディーエム | Transfusion solution generator and transfusion solution production method, and transfusion solution |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102021128006A1 (en) | 2021-10-27 | 2023-04-27 | Eric Keogh | Fuel processing device and system with a fuel processing device and a combustion unit |
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