WO1994019285A1 - Detergent-free cleansing water, process and apparatus for producing the cleansing water, and method of separating emulsion formed by using the cleansing water into water and oil - Google Patents
Detergent-free cleansing water, process and apparatus for producing the cleansing water, and method of separating emulsion formed by using the cleansing water into water and oil Download PDFInfo
- Publication number
- WO1994019285A1 WO1994019285A1 PCT/JP1994/000272 JP9400272W WO9419285A1 WO 1994019285 A1 WO1994019285 A1 WO 1994019285A1 JP 9400272 W JP9400272 W JP 9400272W WO 9419285 A1 WO9419285 A1 WO 9419285A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- metal
- oil
- ion
- exchange resin
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/047—Breaking emulsions with separation aids
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46176—Galvanic cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
- C02F2001/425—Treatment of water, waste water, or sewage by ion-exchange using cation exchangers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
Definitions
- the present invention relates to a washing water for removing dirt such as oil without using a detergent, a method and a manufacturing apparatus for producing the washing water, and a water emulsified by removing dirt such as oil using the washing water as oil.
- the present invention relates to a method for separating water and oil, which separates into water without containing oil.
- the hard-to-remove dirt attached to products and parts in factories and the dirt from clothes, dishes and bathtubs at home generally contain oil, and the dirt containing oil has been conventionally washed off with detergent and water.
- the detergent contains a surfactant in an amount of 20% or more, and the water from which oil stains have been removed by the surfactant causes an emulsifying action called an OZW type emulsion or a W / 0 type emulsion.
- water used to wash products and parts in factories generally contains an anti-sinus agent. This is because when washing with ordinary water such as tap water or well water (generally hard water), Ca 2+ or Mg 2+ or This is because metal ions such as F e 2 + are contained in water. After cleaning products and parts with this detergent containing anti-stopping agents (even for detergents without anti-stopping agents), the products and parts had to be rinsed again with clean water. For this reason, the cost of the anti-sinusoid was expensive, and rinsing was necessary.
- the present invention has been made in view of this point, and provides a washing water capable of removing dirt such as oil without using a detergent, and a method and an apparatus for easily producing the washing water at low cost.
- the purpose is to do.
- Another object of the present invention is to provide a method for easily and immediately separating water emulsified by removing dirt such as oil with water containing no surfactant, and immediately separating the oil into water containing no oil.
- a method for producing cleaning water according to the present invention is such that water is sequentially passed through an ion exchange resin and a mixture of tourmaline and a metal.
- the apparatus for producing wash water according to the present invention includes: a soft water generator accommodating an ion exchange resin therein; and an ion generator accommodating a mixture of tourmaline and metal therein.
- the water passing through the vessel is injected into tourmaline and metal by water pressure to stir the tourmaline and metal in the ion generator.
- the method for separating washing water emulsified by removing oil stains by using the washing water according to the present invention into oil and water containing no oil comprises mixing ion-exchange resin, tourmaline and metal. Oil dirt is removed with the washing water that has been 'passed in the order of water', the oil dirt is removed, and the emulsified washing water is mixed with hard water.
- the washing water according to the present invention is water that has been passed through water such as tap water in the order of ion-exchange resin, tourmaline and metal.
- water such as tap water in the order of ion-exchange resin, tourmaline and metal.
- softened water in generator which incorporates an ion-exchange resin, together with removal of C a 2+ or Mg 2 + and F e 2+, etc. of the metal ions to soft water water, there is a detergency in water generating a human Doroniumuion (H 3 0+).
- the soft water is passed through an ion generator containing tourmaline and a metal. Yotsute thereto, the Hidoroniu Ion (H 3 0+) further together to generate hydroxyl Io emissions (Eta 3 0) the detergency is also a large amount wash water generated.
- Detergency is hydro Niu-ion (H 3 0+) and hydroxy Louis on the detergency is ( ⁇ 3 0 2 ") wash water having a large amount may drop the oil stains, after the oil and drop Water emulsifies.
- the oil stains emulsified water dropped has become a Emarujiyon of OZW type, when the emulsified water this is usually mixed with water such as tap water, hydro two Umuion that encloses an oil (H 3 0 *) also changes to hydroxyl ions (H 3 0 2 ”) is also water, oil is released from the hydro Niu-ion (H 3 0 *) Ya hydroxyl ions (H 3 0 2 '), is separated into oil and water.
- FIG. 1 is a configuration diagram showing an embodiment of a water producing apparatus having a purification activity according to the present invention
- FIG. 2 is a cross-sectional view of a soft water generator used in the producing apparatus shown in FIG. 1
- FIG. FIG. 2 is a sectional view of a main part of the ion generator used in the manufacturing apparatus shown in FIG.
- FIG. 1 is a configuration diagram showing an embodiment of a water producing apparatus having a purifying activity according to the present invention.
- the first soft water generator 10, the second soft water generator 12, and the ion generator 14 are sequentially connected via communication pipes 18 a and 18 b.
- water having a pressure such as tap water
- water having a pressure is supplied from the water supply pipe 20 to the first soft water generator 10 via the communication pipe 22.
- An inlet open / close valve 24 such as a faucet is provided between the water supply pipe 20 and the communication pipe 22, and a check valve 26 is provided in the middle of the communication pipe 22.
- a discharge pipe 28 is provided at the outlet side of the ion generator 14.
- An outlet opening / closing valve 30 is provided at the end of or in the middle of the discharge pipe 28.
- the first soft water generator 10 and the second soft water generator 12 contain a large amount of granular ion exchange resin 32 therein, and their cross-sectional views are shown in FIG.
- the main body 34 of the water softeners 10 and 12 has a cylindrical shape, and has water inlets and outlets 36a and 36b on the upper and lower end surfaces of the cylindrical shape.
- shield members 38a and 38b each having a hole at the center are provided on the inner wall at positions slightly apart from the upper and lower end surfaces.
- the ion-exchange resin 32 is housed in a fine mesh 40 between the pair of shield members 38a and 38b.
- Upper and lower access ⁇ A shield member 38 with a hole in the center is provided on the inner wall at a position slightly away from 36a and 36b because the ion exchange resin 32 is a fine mesh 40 and a pair of shield members. This is for the purpose of forming the spaces 42a and 42b near the entrances and exits 36 & and 36b.
- the reason for allowing water to enter and exit through the central holes of the shield members 38a and 38b is to ensure that the water contacts the ion exchange resin 32.
- the reason why the ion-exchange resin 32 is put into the net 40 is that the granular ion-exchange resin 32 can be taken out together with the net 40 when the granular ion-exchange resin 32 is taken out for cleaning. is there.
- the first soft water generator 10 and the second soft water generator 12 have a height of, for example, 80 cm and an inner diameter of 10 cm. Then, for example, the storage height of the ion exchange resin 32 is set to 7 Ocm (spaces 42 a and 42 b are present above and below). At this time, the storage height of the ion-exchange resin 3'2 needs to be at least such that the ion exchange can be sufficiently performed. On the other hand, if the storage height of the ion exchange resin 32 becomes too high (for example, if the storage height of the ion exchange resin 32 becomes about 200 cm or more), the ion exchange resin 32 becomes less resistant to water. Flow through the interior of the soft water generator Set the storage height of the exchange resin 32 to a level where the flow rate does not decrease. ⁇
- the reason for dividing the container that stores the ion exchange resin 32 into two is that the height of the first soft water generator 10 and the second soft water generator 12 is the same height as the ion generator 14. This is to prevent the flow rate from decreasing due to the pressure loss of the water passing therethrough. It is also possible to combine the two soft water generators 10 and 12 into one to form one soft water generator.
- the inner diameter of the soft water generator, the storage height of the ion exchange resin 32, and the number of soft water generators connected in series can be arbitrarily set according to the flow rate of water.
- the ion exchange resin 32 is for removing metal ions such as Ca 2+, Mg 2+, and Fe 2+ contained in water to make water soft.
- the ion exchange resin 3 2, for example,.
- the ion exchange resin 32 causes the following ion exchange reaction with metal ions such as Ca 2+ , Mg 2+, and Fe 2+ contained in water.
- the ion exchange resin 32 By using strongly acidic force thione exchange resin (R z S 0 3 N a ) as the ion exchange resin 32, the sodium ions in the water (N a +) is generated.
- the ion exchange resin 32 may be one that generates something other than Na +, but one that generates Na + is more preferable.
- FIG. 14 a partial cross-sectional view of the ion generator 14 is shown in FIG.
- the ion generator 14 is formed by connecting a plurality of cartridges 44 in the same arrangement and continuously in a vertical direction. Inside each cartridge 44, a granular tourmaline 46 and a plate-like metal 48 are housed.
- Tourmaline has a brass electrode and a negative electrode.
- the brass electrode and the negative electrode cause water to have an electromagnetic wave having a wavelength of 4 to 14 microns, and cut water clusters to form hydronium. it is of order to generate Ion (H 3 0+).
- the energy of the electromagnetic wave having a wavelength of 4 to 14 microns is 0.004 watt / cm 2 .
- tourmaline 46 may be finely crushed tourmaline stone, but the weight ratio of tourmaline, ceramic and aluminum oxide (some of which contain silver) is about 10:80:10.
- a commercially available tourmaline pellet may be used. The ceramic contained in this tourmaline pellet acts to keep the brass and negative electrodes separate.
- tourmaline 46 is mixed with ceramic at a weight ratio of 5% or more to 800. By heating at C or higher, children can produce traumarin 46, which disappears in a predetermined period (eg, about 3 months in diameter of 4 mm) by stirring water.
- the metal 48 at least one metal of aluminum, stainless steel, and silver is used.
- the metal 48 is preferably a metal that does not produce a feeder in water or dissolve in water.
- aluminum has a bactericidal and antibacterial effect
- Stainless steel has a bactericidal and antibacterial action, as well as a bactericidal and antibacterial action
- silver has a bactericidal and antibacterial action.
- Silver has a stronger bactericidal and antibacterial action than aluminum and stainless steel. For example, if bleaching action is required and more bactericidal or antibacterial action is desired, silver can be mixed with aluminum. Copper and lead cannot be used as metal 48 because of their toxicity. In addition, expensive materials such as gold cannot be adopted from the viewpoint of cost.
- the weight ratio between the tourmaline 46 and the metal 48 is preferably about 10: 1 to 1:10.
- the weight ratio of tourmaline 46 to metal 48 is 1: 2 to 1: 6.
- the weight ratio of tourmaline pellets to metal 48, with the weight ratio of tourmaline, ceramic, and aluminum oxide being about 10:80:10, is 5: 1 to 5: 2.
- the weight ratio is hydro Niu-ion (H 3 0 *) and hydrate Rokishiruion (H 3 0 2 -) is taken into consideration in terms of the incidence of.
- the cartridge 44 has a cylindrical shape with one end opened, and a plurality of holes 52 are provided on a bottom surface 50 thereof.
- the size of the hole 52 is set so that the tourmaline 46 and the metal 48 do not pass through the hole 52 on the bottom surface 50. Set.
- each cartridge 44 has a bottom surface 50 provided with a number of holes 52 facing down, and a tourmaline 46 and a metal 48 are placed on the bottom surface 50. Then, it is set so that the inside of each cartridge 44 flows from the lower part to the upper part. That is, in each of the cartridges 44, the water that has passed through the many holes 52 on the bottom surface 50 is set to be jetted upward from the bottom toward the tourmaline 46 and the metal 48.
- tap water has a high water pressure
- the water having the water pressure vigorously collides with the tourmaline 46 and the metal 48 in the cartridge 44, and the force of the water causes the tourmaline 46 and the metal 48.
- the size and number of the holes 52 are set so that the water is stirred in the cartridge 44. Tourmaline 4 6 and metal 4 8 using the momentum through which water passes Various methods are conceivable as a method for stirring the mixture in the cartridge 44, but any conventionally known stirring means may be used.
- the electrode is dissolved into water by cutting the cluster of water, heat Doroyuumuion (H 3 0 + ) and hydroxyl ions ( ⁇ 3 0) and is due to the large amount of outgoing produced. Also, by injecting pressurized water such as tap water into the tourmaline or the like from below through the hole 52, it is not necessary to provide a search means.
- cartridges 44 each having an inner diameter of 6 cm and a depth of 9 cm are stacked in four layers, and the cartridge 44 has sufficient storage for tourmaline 46 and metal 48.
- the amount is such that tourmaline 46 and metal 48 can move freely in cartridge 44.
- the number of stages of the cartridges 44 may be increased or decreased, or one cartridge 44 with a larger storage capacity may be used.
- the tourmaline 46 stored in the cartridge 44 dissolves in water and disappears in a few months.Therefore, each cartridge 44 can be easily attached and detached by means of, for example, screwing. Make tourmaline 46 easily replenishable.
- the metal 48 does not need to be replenished because it does not dissolve in water, but the entire cartridge 44 containing the tourmaline 46 and the metal 48 can be replaced.
- the storage volume of the cartridge 4 may be changed according to the amount of flow used.
- tourmaline 46 has a brass electrode and a negative electrode, when tourmaline is stirred with water, water (H 20 ) dissociates into hydrogen ions (H + ) and hydroxide ions (0 H _). I do.
- hydroxide ions (0H-) will water (H 2 0) and combined with hydroxy Louis on (H 3 0 2 ").
- the hydro, Kishiruion ( ⁇ 3 0 2 ”) has a surface activity like the hydro Niu-ion (H 3 0+), serves to clean the oil dropped or clothes.
- Ion exchange resin 32 passing water, depending on passing the ion generator 14, internal to the hydro Niu-ion water (H 3 0+) and hydroxyl ions (H 3 0 2 ”) and H + and OH- and is generated.
- the chlorine (C 1) that has passed through the ion exchange resin 32 and the Na + generated in the ion exchange resin 32 pass through the ion generator 14 without reacting.
- wash water water that first passed through the ion-exchange resin 32 and then passed through tourmaline 46 and metal 48 (hereinafter, this water is referred to as “wash water”) includes Na +, C and 1-, and H +, and 0H-, the large amount of hydro Niu-ion (H 3 0+), a large amount of hydroxyl ions (H 3 0) and are present.
- the washing water is soft water, and has a specific gravity of about 1.4 to 1.5.
- the wash water has electromagnetic waves of wavelength 4 to 14 microns whose energy is 0.004 watt tZcm 2 .
- This washing water exhibits many effects listed below.
- washing water If used, no detergent is required. Also, this washing ice is not only used as water for washing machines; it can be applied to all household washing fields that use detergents such as dishwashers and bathtubs. In addition, it can also be used to clean oil stains in factories and other parts and products and parts.
- this washing water can be used for industrial and household purposes without using detergent. All washing can be performed, and it is more economical than using washing water and does not cause environmental pollution due to the drainage of washing liquid.
- the wash water Since the wash water is removed C a 2 + and M g 2 + and F e 2 + like metal ions, does not cause ⁇ be washed products and parts in the factory in this cleaning water. Therefore, it is economical because there is no need to mix a preventive agent when cleaning products and parts in a factory. Furthermore, since the washing water does not use a detergent, there is no need to rinse the products and parts with clean water after washing the products and parts, which is economical.
- Tourmaline emits weak energy (electromagnetic waves with wavelengths of 4 to 14 microns). This weak energy cuts large clusters of water (36 to 38 clusters of tap water, 3 to 6 clusters of washing water), and is trapped in the clusters Releases toxic gases and heavy metals from water. That is, toxic gas and heavy metals contained in the water are released, and the water becomes free of impurities. As a result, it can be used for cleaning precision parts.
- Aluminum has a bleaching effect, and if the mixing amount of aluminum is increased, the bleaching effect is obtained during washing.
- hydro Niu-ion (H 3 0 +) Ya hydro Kishiruion (H 3 0 2 -) is to wrap the oil, all types of oil stains chill drop.
- Water that has been cleaned of oil using cleaning water causes emulsification of the ZW type emulsion (a type that encloses hydraulic power oil).
- ZW type emulsion a type that encloses hydraulic power oil.
- the washing water that has become a 0 ZW type emulsion remains. It is prohibited to drain this emulsified washing water as it is.
- a method for separating oil and oil-free water from oil emulsified by removing oil stains using washing water will be described.
- normal water such as tap water or well water
- washing water and normal water are the opposite of soft water and hard water.
- the washing water of the OZW type emulsion that has been cleaned of oil is poured into hard water such as tap water. Put a large amount of tap water in the container, and put the washing water of the 0 / W type emulsion that has been cleaned of oil dirt into it.
- Hard water such as tap water may be added to the washing water of the 0 / W type emulsion, but 0 / W type can be added to normal water in terms of promoting the separation of water and oil. It is preferable to add the emulsion water.
- hydroxyl ions are wrapped oil (H 3 0 2 -) since the hydro two Umuion (H 3 0 +) is water, oil hydroxyl ions (H 3 0 2 -) Ya hydro Niu-ion ( H 3 0 + ), resulting in separation of oil and oil-free water.
- the washing water of oil-stained 0ZW type emulsion is poured into hard water such as tap water to immediately separate oil and oil-free water. As described above, the oil and the water containing no oil are separated into two layers, so that the subsequent removal of the oil can be easily performed.
- wash water is simply passed through the mixture of tourmaline and metal next to the ion exchange resin, and the production cost of wash water is low. It is. Also, the manufacturing equipment is a simple one using water power and does not use electricity, so the manufacturing equipment is inexpensive. Further, in the manufacturing apparatus of the present invention, it is only necessary to clean or replenish the material, so that there is no need for maintenance, and anyone can clean or replenish the material. In the present invention, the washing water emulsified by removing dirt such as oil with the washing water is simply poured into ordinary water such as tap water to be immediately separated into ordinary water and oil. Therefore, the conventional expensive apparatus for separating water and oil is not required, and the separation of water and oil can be achieved at low cost, easily and quickly.
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- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Washing And Drying Of Tableware (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Cosmetics (AREA)
- Detergent Compositions (AREA)
- Physical Water Treatments (AREA)
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019950703460A KR100206312B1 (ko) | 1993-02-26 | 1994-02-23 | 세제를 사용하지 않은 세정수와,그 세정수의 제조방법과 그 제조장치, 및 유화된 것을 물과 기름으로 분리하는데 그 세정수를 사용하는 방법 |
US08/495,400 US5599455A (en) | 1993-02-26 | 1994-02-23 | Detergent-free washing water, method and apparatus for making the washing water, and water/oil separation method for separating matters emulsified with the washing water into water and oil phases |
EP94907660A EP0686602A4 (en) | 1993-02-26 | 1994-02-23 | DETERGENT-FREE CLEANING WATER, METHOD AND DEVICE FOR PRODUCING THE CLEANING WATER AND METHOD FOR SEPARATING AN EMULSION IN WATER AND OIL, MADE BY USE OF THE CLEANING WATER |
CA002155742A CA2155742C (en) | 1993-02-26 | 1994-02-23 | Detergent-free washing water, method and apparatus for making the washing water, and water/oil separation method for separating matters emulsified with the washing water into water and oil phases |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5/12717U | 1993-02-26 | ||
JP1271793 | 1993-02-26 | ||
JP6/23066 | 1994-01-25 | ||
JP02306694A JP3170132B2 (ja) | 1993-02-26 | 1994-01-25 | 洗剤を使用しない洗浄水と、その洗浄水の製造方法並びにその製造装置、及びその洗浄水を使用して乳化したものを水と油に分離する水と油の分離方法 |
Publications (1)
Publication Number | Publication Date |
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WO1994019285A1 true WO1994019285A1 (en) | 1994-09-01 |
Family
ID=26348363
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1994/000272 WO1994019285A1 (en) | 1993-02-26 | 1994-02-23 | Detergent-free cleansing water, process and apparatus for producing the cleansing water, and method of separating emulsion formed by using the cleansing water into water and oil |
Country Status (6)
Country | Link |
---|---|
US (1) | US5599455A (ja) |
EP (1) | EP0686602A4 (ja) |
JP (1) | JP3170132B2 (ja) |
KR (1) | KR100206312B1 (ja) |
CA (1) | CA2155742C (ja) |
WO (1) | WO1994019285A1 (ja) |
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JP2889903B2 (ja) * | 1993-11-09 | 1999-05-10 | 利春 深井 | 浄化活性作用を有する水の製造方法及び製造装置 |
US6219871B1 (en) | 1997-04-14 | 2001-04-24 | Max B. Frederick | Washing apparatus and method utilizing flexible container to improve cleaning efficiency and minimize space occupancy |
JP3121287B2 (ja) * | 1997-04-17 | 2000-12-25 | クランツ株式会社 | 水浄化装置 |
US6034013A (en) * | 1998-03-12 | 2000-03-07 | Mino Ganryo Kagaku Corporation | Tourmaline composite grains and apparatus using them |
US6036965A (en) * | 1998-03-13 | 2000-03-14 | Color Access, Inc. | Tourmaline in cosmetic cleansing compositions |
US6308356B1 (en) | 1998-04-01 | 2001-10-30 | Max B. Frederick | Substantially environmental-pollution-free cleaning method and device employing electric energy and surface physical properties |
DE60035473T2 (de) | 1999-12-08 | 2008-03-13 | Nipro Corp. | Leicht abziehbare Folie und medizinischer Verpackungsbehälter |
JP2001347274A (ja) * | 2000-04-04 | 2001-12-18 | Kokichi Aoki | 水質改良剤、水質改良装置及び同装置の利用方法 |
US20060180550A1 (en) * | 2005-02-16 | 2006-08-17 | Metal & Arsenic Removal Technology | Portable water purifier |
JP4939077B2 (ja) * | 2006-02-23 | 2012-05-23 | 利春 深井 | 水に含まれるアスベストの除去方法及びその除去装置 |
WO2008113151A1 (en) * | 2007-03-21 | 2008-09-25 | Wei He | Far-infrared ray composite material, method of producing the same, and method for liquid or water filtration |
JP4551944B2 (ja) * | 2007-05-15 | 2010-09-29 | 利春 深井 | 油分乳化物 |
JP2009165940A (ja) * | 2008-01-15 | 2009-07-30 | Toshiharu Fukai | 過飽和溶存酸素を含む水の製造方法 |
DE102008023228A1 (de) | 2008-05-08 | 2009-11-19 | Technische Universität Dresden | Nanopartikel zur selektiven Gewebetherapie, Verfahren zu deren Herstellung und deren Verwendung in der Gewebetherapie |
DE102008030035A1 (de) | 2008-06-18 | 2010-02-04 | Technische Universität Dresden | Verfahren zur Durchführung heterogen katalysierter chemischer Reaktionen sowie zur Steuerung von Phasenumwandlungsprozessen |
US20130039846A1 (en) * | 2010-04-27 | 2013-02-14 | Toshiharu Fukai | Method for producing hydrogen |
WO2011136147A1 (ja) * | 2010-04-27 | 2011-11-03 | Fukai Toshiharu | 水素の製造方法 |
US10302605B2 (en) | 2011-02-07 | 2019-05-28 | Agilent Technologies, Inc. | Column assembly for a gas chromatograph |
CN109791129A (zh) * | 2016-06-28 | 2019-05-21 | 珀金埃尔默健康科学有限公司 | 改进的低热质gc模块 |
KR102040401B1 (ko) * | 2018-05-14 | 2019-11-05 | 채효순 | 액상소금을 이용한 클린룸 및 그 시스템 |
IT201900010233A1 (it) * | 2019-06-27 | 2020-12-27 | Corrado Chierroni | Dispositivo per il trattamento dell’acqua di alimentazione di una lavatrice |
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JPH01284387A (ja) * | 1988-05-12 | 1989-11-15 | Jiyunsui Service:Kk | カリウム水製造装置 |
JPH03101892A (ja) * | 1989-09-13 | 1991-04-26 | Kamioka Kogyo Kk | 水処理方法及び装置 |
JPH0445593U (ja) * | 1990-08-17 | 1992-04-17 | ||
JPH04141292A (ja) * | 1990-09-29 | 1992-05-14 | Nobuo Hirasawa | 水活性化作用を有する粉体の製造方法 |
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US4483756A (en) * | 1982-09-27 | 1984-11-20 | Atlantic Richfield Company | Method of applying electrical energy to a reactant chamber |
JPH0738987B2 (ja) * | 1989-10-03 | 1995-05-01 | 有限会社久保技術事務所 | 電気石を用いた水の界面活性化装置および電気石粒状物 |
JPH03249989A (ja) * | 1990-02-27 | 1991-11-07 | Kubo Gijutsu Jimusho:Kk | 電気石結晶によるイオン物質の電着除去方法と金属電着電気石結晶 |
US5108618A (en) * | 1990-10-30 | 1992-04-28 | Nobuo Hirasawa | Method of and apparatus for modifying fuel |
-
1994
- 1994-01-25 JP JP02306694A patent/JP3170132B2/ja not_active Expired - Lifetime
- 1994-02-23 KR KR1019950703460A patent/KR100206312B1/ko not_active IP Right Cessation
- 1994-02-23 CA CA002155742A patent/CA2155742C/en not_active Expired - Fee Related
- 1994-02-23 EP EP94907660A patent/EP0686602A4/en not_active Withdrawn
- 1994-02-23 US US08/495,400 patent/US5599455A/en not_active Expired - Fee Related
- 1994-02-23 WO PCT/JP1994/000272 patent/WO1994019285A1/ja not_active Application Discontinuation
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JPS586524B2 (ja) * | 1978-05-19 | 1983-02-04 | 松下電器産業株式会社 | 含油廃水の処理法 |
JPS605495U (ja) * | 1983-06-23 | 1985-01-16 | 株式会社東芝 | 水中の不純物除去装置 |
JPS61181589A (ja) * | 1985-02-06 | 1986-08-14 | Nippon Paint Co Ltd | 脱イオン純水製造装置 |
JPH01284387A (ja) * | 1988-05-12 | 1989-11-15 | Jiyunsui Service:Kk | カリウム水製造装置 |
JPH03101892A (ja) * | 1989-09-13 | 1991-04-26 | Kamioka Kogyo Kk | 水処理方法及び装置 |
JPH0445593U (ja) * | 1990-08-17 | 1992-04-17 | ||
JPH04141292A (ja) * | 1990-09-29 | 1992-05-14 | Nobuo Hirasawa | 水活性化作用を有する粉体の製造方法 |
Non-Patent Citations (1)
Title |
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See also references of EP0686602A4 * |
Also Published As
Publication number | Publication date |
---|---|
KR100206312B1 (ko) | 1999-07-01 |
CA2155742A1 (en) | 1994-09-01 |
JP3170132B2 (ja) | 2001-05-28 |
CA2155742C (en) | 2000-08-15 |
US5599455A (en) | 1997-02-04 |
JPH0796283A (ja) | 1995-04-11 |
KR960700964A (ko) | 1996-02-24 |
EP0686602A1 (en) | 1995-12-13 |
EP0686602A4 (en) | 1997-03-05 |
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