CN102764605B - The method and apparatus of high-oxygen water is produced in a kind of not electricity consumption - Google Patents
The method and apparatus of high-oxygen water is produced in a kind of not electricity consumption Download PDFInfo
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- CN102764605B CN102764605B CN201210264947.4A CN201210264947A CN102764605B CN 102764605 B CN102764605 B CN 102764605B CN 201210264947 A CN201210264947 A CN 201210264947A CN 102764605 B CN102764605 B CN 102764605B
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- oxygen
- miscible
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- water
- ejector
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- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 99
- 239000001301 oxygen Substances 0.000 title claims abstract description 99
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 238000000034 method Methods 0.000 title claims abstract description 23
- 230000005611 electricity Effects 0.000 title claims abstract description 19
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 70
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 8
- 238000000746 purification Methods 0.000 claims abstract description 8
- 125000006850 spacer group Chemical group 0.000 claims abstract description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims description 17
- 239000010935 stainless steel Substances 0.000 claims description 17
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 238000009792 diffusion process Methods 0.000 claims description 7
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 238000003466 welding Methods 0.000 claims description 7
- 235000013361 beverage Nutrition 0.000 claims description 5
- 239000008399 tap water Substances 0.000 claims description 4
- 235000020679 tap water Nutrition 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 239000008400 supply water Substances 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims 1
- 238000009434 installation Methods 0.000 abstract description 3
- 235000014214 soft drink Nutrition 0.000 abstract description 2
- 235000020188 drinking water Nutrition 0.000 description 4
- 239000003651 drinking water Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000003760 magnetic stirring Methods 0.000 description 3
- 238000005374 membrane filtration Methods 0.000 description 3
- QVGXLLKOCUKJST-NJFSPNSNSA-N oxygen-18 atom Chemical compound [18O] QVGXLLKOCUKJST-NJFSPNSNSA-N 0.000 description 3
- 238000006213 oxygenation reaction Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 241000316986 Scutellathous comes Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000015111 chews Nutrition 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000012858 packaging process Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The invention discloses the method and apparatus that high-oxygen water is produced in a kind of not electricity consumption, it is made up of the miscible device of jet, oxygen-dissolving apparatus, output filling apparatus three part; The miscible device of jet by tank body, intake antrum, Pressure gauge, upper spacer, ejector group, lower clapboard, miscible chamber, liquid level gauge, muff nine part form; Oxygen-dissolving apparatus, by dense oxygen chamber, enters oxygen valve, and oxygen gauge three part forms; Export filling apparatus by current divider, flow divider, workbench three part forms; The tank body of the miscible device of jet adopts upper and lower two dividing plates tank body cavity volume to be separated into intake antrum, dense oxygen chamber and miscible chamber three part; Intake antrum top adopts pipe pipeline to connect water intaking valve, and water intaking valve connects water purification intake line by pipeline again; Each installation ejector in the through hole that upper and lower often pair, dividing plate is relative, composition ejector group; The present invention adopts the miscible method of jet to make whole equipment not have rotatable parts, solves a difficult problem of producing high-oxygen water electricity consumption, is applicable to the application of medium and small Soft Drinks Plant.
Description
Technical field:
The present invention relates to a kind of equipment producing high-oxygen water, particularly the method and apparatus of high-oxygen water is produced in a kind of not electricity consumption, belongs to the technical field of environmental protection water purification industry.
Background technology:
Along with the living standard of people, the raising of prevention consciousness, people have paid close attention to healthy Drinking Water Problem.Since last century the nineties, the U.S. comes into vogue a kind of very special high-oxygen water containing a large amount of oxygen part.After this, directly drink purification high-oxygen water extensively to be approved by society gradually.Now, high-oxygen water has been the internationally recognized senior drinking water more meeting human health demand, Japan grade for some developed countries all regard as high-oxygen water " 21 century optimal drinking water ".Scientific research measures light water and often rises oxygen content at 4 ~ 6 milligrams, and high-oxygen water is exactly that often liter of content of oxygen dissolved in water is higher than light water.At present, method society manufacturing high-oxygen water mainly contains: directly dissolved oxygen gas method and chemical reaction method.Direct oxygen dissolution method is comparatively general, the method be more easily accepted! Chinese patent: " a kind of manufacture method of water containing high dissolved oxygen and the device thereof " of 200910018303.5, its technique is as follows: (1) by water source after sand filter, activated carbon filtration, accurate membrane filtration, high-accuracy membrane filtration, reverse osmosis membrane filtration, send into the opening cylinder in the tank body manufacturing water containing high dissolved oxygen device, medical high purity oxygen is sent in tank body simultaneously; (2) open the magnetic stirring apparatus in tank body inner opening cylinder bottom portion, oxygen is fully contacted with water; (3) water containing high dissolved oxygen flows out from tank base delivery port, ultraviolet C sterilization, bottling, it is characterized in that: be provided with opening cylinder body in the bottom of tank body, cylinder base is provided with the magnetic stirring apparatus of band stirring vane, magnetic stirring apparatus is connected with the motor of tank base, and the top of tank body is provided with oxygen inlet, water inlet, feed inlet, and the bottom of tank body is provided with water containing high dissolved oxygen outlet.The utility model of Chinese patent: 201120194974.X relates to the equipment preparing oxygen-added drinks, comprise the vertical tank body of stainless steel, the vertical tank body of stainless steel is the cylindrical shell of seal welding, the bottom of cylindrical shell is provided with supporting leg, be provided with rotatable straight tube and compressor in cylindrical shell, rotatable straight tube be provided with oxygenation dish, motor and transmission device are connected with rotatable straight tube, the outlet of spiral coil is communicated with rotatable straight tube with oxygen hose, and the lower end of cylindrical shell is provided with tap hole.Beneficial effect is: be provided with vacuum heat-insulating layer in equipment surface, and straight tube rotates and be provided with multiple oxygenation dish on straight tube in oxygenation process, carry out multistage oxygenated treatment simultaneously, structure is simple, easy to operate, improve the dissolved efficiency of oxygen, add the content of oxygen in beverage, extend the service life of equipment.Above-mentioned 2 patent formula complex structures, adopt electric power, are inconvenient to promote! Chinese patent: " a kind of generation oxygen-enriched water apparatus " of 03249983.3, it comprises jet pipe, oxygen supply chews core, static mixer composition, it is characterized in that: jet pipe port of export when there being WATER AS FLOW MEDIUM to flow through has a negative pressuren zone to be formed, the malleation oxygen that just in time oxygen supply being positioned at this region being chewed core provides sucks, the gas-liquid mixed media now produced fully mixes through static mixer, and former water oxygen content is increased.Chinese patent: " heavy-oxygen-enriched water and packaging process and container " of 200710022699.1, disclose heavy-oxygen-enriched water by pure water with pure oxygen is filling forms in a reservoir, pure water accounts for the 50-70% of vessel volume, and pure oxygen accounts for the 30-50% of vessel volume.The inner cap of the container filling of this heavy-oxygen-enriched water is arranged on the bottleneck of bottle, enclosing cover covers in being sealed in, wherein, cover in described and fix a drainpipe and gas tube, one end of drainpipe is positioned at outside inner cap, the other end of drainpipe inserts the 50-70% place being positioned at the volume of bottle in bottle, and one end of gas tube is positioned at outside inner cap, and the other end of gas tube inserts distance bottle body bottom 1-2mm in bottle.Above-mentioned two schemes structure is simple, and dissolved oxygen concentration is not high!
Summary of the invention:
The object of this invention is to provide the method and apparatus that high-oxygen water is produced in a kind of not electricity consumption, it is by adopt with the following method and device realizes: running water water source relies on pressure of supply water that the water through purification is input to the miscible device top of jet, when pressure flow is diverted through the ejector group of several ejectors composition again, due to the effect of each ejector, negative pressure is produced in the dense oxygen chamber of each ejector air inlet pipe place oxygen-dissolving apparatus, by the oxygen in the dense oxygen chamber of oxygen-dissolving apparatus suck and miscible with current, and continue miscible in the miscible chamber being ejected into the miscible device of jet together along with the current of ejector diffusion spout, realizing pressure flow and oxygen is fully miscible, finally again through exporting filling apparatus, still relying on the pressure in miscible chamber to carry out packing to beverage bottle.Like this, the non-electric object of production high-oxygen water is just completed.
The equipment that high-oxygen water is produced in a kind of not electricity consumption of the present invention is made up of the miscible device of jet, oxygen-dissolving apparatus, output filling apparatus three part; The miscible device of jet by tank body, intake antrum, Pressure gauge, upper spacer, ejector group, lower clapboard, miscible chamber, liquid level gauge, muff nine part form; Oxygen-dissolving apparatus, by dense oxygen chamber, enters oxygen valve, and oxygen gauge three part forms; Export filling apparatus by current divider, flow divider, workbench three part forms.The tank body of the miscible device of jet adopts upper and lower two dividing plates to be welded and fixed, and tank body cavity volume is separated into intake antrum, dense oxygen chamber and miscible chamber three part.
The production technology that the equipment of high-oxygen water is produced in a kind of not electricity consumption of the present invention is: the tank body of the miscible device of jet adopts stainless steel materials to be processed into the pressure-vessel tank shape meeting national Specification, and the thickness of stainless steel materials is selected between 1--10 millimeter; Two ends end socket also adopts the pressure-vessel standard sealing head meeting national Specification, thickness is selected between 2-10 millimeter, respectively process a through hole at upper and lower end socket and weld section of a pipe, upper end pipe is connected with water intaking valve pipeline, lower end pipe pipeline connects the current divider exporting filling apparatus, the diameter of above-mentioned pipe select should with running water water source same diameter or the pipe that is less than tap water source diameter; In the chamber of the tank body of the miscible device of jet, weld upper and lower two pieces of stainless steel thick plates as dividing plate, thickness is selected between 3-12 millimeter, and tank body cavity volume is separated into intake antrum, dense oxygen chamber and miscible chamber three part by dividing plate; Intake antrum upper weld upper cover, welds low head below miscible chamber, is dense oxygen chamber between upper and lower dividing plate; Need according to flow the through hole processing equal number in upper and lower dividing plate centre, the selection principle of number of openings is the sectional area that the summation of the ejector water inlet sectional area used of ejector group should be equal to or less than running water water source water inlet pipe, such selection can improve the water velocity by ejector, ejector air inlet is made to produce larger suction, and making the through hole of processing, hole, hole is relative; Install in the through hole that upper and lower often pair, dividing plate is relative and fix an ejector, also must make the intake antrum of ejector water inlet on upper spacer, the dense oxygen chamber of ejector air inlet between upper and lower dividing plate, the ejector diffusion miscible chamber of spout below lower clapboard, composition ejector group.Adopt the object of ejector group to be the contact area of increase pressure flow and air inlet and facilitate Standardization instrument to produce; A through hole processed respectively by the chamber wall in intake antrum, miscible chamber and dense oxygen chamber, the stainless steel nut that in through hole, welding one is supporting with pressure gauge base, for distinguishing setting pressure table; At the through hole that the upper and lower each processing one of the chamber wall in miscible chamber is supporting with liquid level gauge, the stainless steel nut that in through hole, each welding one is supporting with liquid level gauge, for installation liquid level gauge; The muff of a set of employing insulation material composition is also installed at the tank body outer surface of the miscible device of jet.
The Pressure gauge of the equipment of high-oxygen water is produced in a kind of not electricity consumption of the present invention, ejector, and liquid level gauge, enters oxygen valve, current divider, and flow divider is all general national standard accessory, and workbench adopts the table type workbench of metal or timber processing.
Before the equipment work of high-oxygen water is produced in a kind of not electricity consumption of the present invention, first water intaking valve pipeline is connected through the running water water source of purification, the medical oxygen source of the gas that oxygen valve pipeline is connected through decompression is entered again by dense oxygen chamber, dense oxygen chamber is made to be full of abundant oxygen, observe oxygen gauge, control between 0.1-0.8 MPa; During work, open water intaking valve.Press water flows into intake antrum, and shunting enters from each ejector water inlet of ejector group, from the ejection of ejector diffusion spout, due to the effect of each ejector, negative pressure is produced in the dense oxygen chamber of each ejector air inlet pipe place oxygen-dissolving apparatus, the oxygen in the dense oxygen chamber of oxygen-dissolving apparatus to be sucked and miscible with current, continue miscible in the miscible chamber being ejected into the miscible device of jet together along with the current of ejector diffusion spout; Last again through exporting filling apparatus, still rely on the pressure in miscible chamber to carry out packing to beverage bottle.Like this, the non-electric object of production high-oxygen water is just completed.
The present invention produces the method and apparatus of high-oxygen water owing to adopting above-mentioned a kind of not electricity consumption, and improve the dissolved oxygen of drinking water, and occupation area of equipment is few, structure is simple.Owing to adopting the miscible method of jet to make whole equipment not have rotatable parts, not electricity consumption, solve and produce the low difficult problem of high-oxygen water dissolved oxygen, and equipment operating is very easy, maintains easily, cost is also lower, and economic benefit is very remarkable.Be particularly suitable for the application of medium and small Soft Drinks Plant, be easily easily accepted by a user, facilitate penetration and promotion.
Accompanying drawing illustrates:
Below in conjunction with drawings and Examples, the present invention is further described:
Fig. 1 is embodiments of the invention: the structural representation of the method and apparatus of high-oxygen water is produced in a kind of not electricity consumption.
Fig. 2 is Fig. 1 embodiment: concrete structure and the schematic flow sheet of the method and apparatus of high-oxygen water are produced in a kind of not electricity consumption.
In figure: 1, the miscible device of jet; 2, oxygen-dissolving apparatus; 3, filling apparatus is exported; 10, intake antrum, 11, miscible chamber, 12, Pressure gauge, 13, upper spacer, 14 dense oxygen chambeies, 15, ejector group, 16, ejector water inlet, 17, ejector air inlet, 18, ejector diffusion spout, 19, lower clapboard, 20, liquid level gauge, 21, enter oxygen valve, 22, oxygen gauge, 23, muff, 31, current divider, 32, flow divider, 33, beverage bottle, 34, workbench, it is flow direction of purifying waste water that solid arrow guides; Dash-dot arrows is guided as oxygen flow direction.
Detailed description of the invention:
Reference Fig. 1, Fig. 2 are a kind of embodiments of the present invention: the method and apparatus of high-oxygen water is produced in a kind of not electricity consumption, choosing source is through the city tap-water of purification, pipeline water inlet pipe diameter 32 millimeters, intake pressure 0.3-0.4 MPa, the ejector of ejector group selects 2, produces high-oxygen water flow and selects 2 tons per hour.The concrete structure of embodiment: be made up of the miscible device 1 of jet, oxygen-dissolving apparatus 2, output filling apparatus 3 three part; The miscible device 1 of jet by tank body, intake antrum 10, Pressure gauge 12, upper spacer 13, ejector group 15, lower clapboard 19, miscible chamber 11, liquid level gauge 20, muff 23 9 part form; Oxygen-dissolving apparatus 2, by dense oxygen chamber 14, enters oxygen valve 21, and oxygen gauge 22 3 part forms; Export filling apparatus 3 by current divider 31, flow divider 32, workbench 34 3 part forms.
The production technology that the apparatus embodiments of high-oxygen water is produced in a kind of not electricity consumption of the present invention is: the tank body of the miscible device 1 of jet adopts stainless steel materials to be processed into the pressure-vessel tank shape meeting national Specification, diameter selects 273 millimeters, and the thickness of stainless steel materials selects 3 millimeters; Two ends end socket adopts the pressure-vessel standard sealing head meeting national Specification, diameter 273 millimeters, thickness is at 3.5 millimeters, upper and lower two dividing plates 13,19 that the tank body cavity volume of the miscible device of jet 1 adopts the stainless steel materials of 3 mm of thickness to process are welded in tank body cavity volume, just the cavity volume of tank body are separated into intake antrum 10, dense oxygen chamber 14 and miscible chamber 11 3 part; Intake antrum 10 top adopts the pipe of diameter 25 millimeters, and pipeline connects 25 millimeters of ball water intaking valves, and ball water intaking valve connects city tap-water water purification intake line by pipeline again; Upper and lower every, 13,19 centres need the through hole of processing 2 diameters 20 millimeters of same sizes according to flow, and make the through hole of processing, hole, hole is relative; And the ejector fixing a diameter 20 millimeters is installed in often pair of upper and lower dividing plate 13,19 relative through hole, also must make in the intake antrum 10 of 2 ejector water inlets 16 on upper spacer 13, in 2 ejector air inlets 17 dense oxygen chamber 14 between upper and lower dividing plate 13,19,2 ejectors spread in the miscible chamber 11 of spout 18 below lower clapboard 19, composition ejector group 15; A through hole being processed respectively by the chamber wall in intake antrum 10, miscible chamber 11 and dense oxygen chamber 14, in through hole, welding a stainless steel nut supporting with pressure gauge base, for distinguishing setting pressure table 12 and oxygen gauge 22; At the through hole that the upper and lower each processing one of the chamber wall in miscible chamber 11 is supporting with liquid level meter, the stainless steel nut that each welding one is supporting with liquid level gauge in through hole, for installation liquid level gauge 20; The muff 23 of a set of employing foamed plastic is also installed at the tank body outer surface of the miscible device of jet 1.
The Pressure gauge 12 of the apparatus embodiments of high-oxygen water is produced in a kind of not electricity consumption of the present invention, oxygen gauge 22, ejector, liquid level gauge 20, enters oxygen valve 21, current divider 31, flow divider 32 is all general national standard accessory, and workbench 34 adopts metal solder to be processed into a type workbench.
Claims (3)
1. the method for a not electricity consumption production high-oxygen water, it is characterized in that: it adopts running water water source, rely on pressure of supply water that the water through purification is input to the miscible device top of jet, the ejector group that pressure flow consists of several ejectors, and spray, be diffused in the miscible chamber of jet miscible device bottom, when the current purified are by ejector group, due to the effect of each ejector, negative pressure is produced in the dense oxygen chamber of each ejector air inlet pipe place oxygen-dissolving apparatus, by the oxygen in the dense oxygen chamber of oxygen-dissolving apparatus suck and miscible with current, continue miscible in the miscible chamber being ejected into the miscible device of jet together along with the current of ejector diffusion spout, realize pressure flow and oxygen is fully miscible, last again through exporting filling apparatus, still the pressure in miscible chamber is relied on to carry out packing to beverage bottle, like this, just complete and produce the non-electric object of high-oxygen water.
2. an equipment for high-oxygen water is produced in not electricity consumption, it is characterized in that: the tank body of the miscible device of jet adopts stainless steel materials to be processed into the pressure-vessel tank shape meeting national Specification, and the thickness of stainless steel materials is selected between 1--10 millimeter; Two ends end socket also adopts the pressure-vessel standard sealing head meeting national Specification, thickness is selected between 2-10 millimeter, respectively process a through hole at upper and lower end socket and weld section of a pipe, upper end pipe is connected with water intaking valve pipeline, lower end pipe pipeline connects the current divider exporting filling apparatus, the diameter of above-mentioned pipe select should with running water water source same diameter or the pipe being less than tap water source diameter; In the chamber of the tank body of the miscible device of jet, weld upper and lower two pieces of stainless steel thick plates as dividing plate, thickness is selected between 3-12 millimeter, and tank body cavity volume is separated into intake antrum, dense oxygen chamber and miscible chamber three part by dividing plate; Intake antrum upper weld upper cover, welds low head below miscible chamber, is dense oxygen chamber between upper and lower dividing plate; Need according to flow the through hole processing equal number in upper and lower dividing plate centre, the selection principle of number of openings is the sectional area that the summation of the ejector water inlet sectional area used of ejector group should be equal to or less than running water water source water inlet pipe, and making the through hole of processing, hole, hole is relative; Install in the through hole that upper and lower often pair, dividing plate is relative and fix an ejector, also must make the intake antrum of ejector water inlet on upper spacer, the dense oxygen chamber of ejector air inlet between upper and lower dividing plate, the ejector diffusion miscible chamber of spout below lower clapboard, composition ejector group; A through hole processed respectively by the chamber wall in intake antrum, miscible chamber and dense oxygen chamber, the stainless steel nut that in through hole, welding one is supporting with pressure gauge base; At the through hole that the upper and lower each processing one of the chamber wall in miscible chamber is supporting with liquid level gauge, the stainless steel nut that welding one is supporting with liquid level gauge in through hole; The muff of a set of employing foamed plastic composition is also installed at the tank body outer surface of the miscible device of jet.
3. the equipment required by claim 2, is characterized in that: the Pressure gauge adopted, ejector, and liquid level gauge enters oxygen valve, current divider, and flow divider is all general national standard accessory, and workbench is the table type workbench adopting metal or timber processing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201210264947.4A CN102764605B (en) | 2012-07-30 | 2012-07-30 | The method and apparatus of high-oxygen water is produced in a kind of not electricity consumption |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201210264947.4A CN102764605B (en) | 2012-07-30 | 2012-07-30 | The method and apparatus of high-oxygen water is produced in a kind of not electricity consumption |
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| CN102764605A CN102764605A (en) | 2012-11-07 |
| CN102764605B true CN102764605B (en) | 2015-09-30 |
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| CN201210264947.4A Expired - Fee Related CN102764605B (en) | 2012-07-30 | 2012-07-30 | The method and apparatus of high-oxygen water is produced in a kind of not electricity consumption |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104129863A (en) * | 2014-07-19 | 2014-11-05 | 朱建林 | Continuous repeated circulation clear-water oxygenation device |
| CN104556435A (en) * | 2015-01-19 | 2015-04-29 | 黄志昌 | Centrifugal pump internal/external cyclic centrifugal oxygenation device |
| CN115382413A (en) * | 2022-09-26 | 2022-11-25 | 青岛涌源水务环境科技有限公司 | Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system |
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| CN1112457A (en) * | 1994-03-15 | 1995-11-29 | 英国氧气集团有限公司 | Gas dissolving |
| US5842600A (en) * | 1996-07-11 | 1998-12-01 | Standex International Corporation | Tankless beverage water carbonation process and apparatus |
| CN201244454Y (en) * | 2008-08-20 | 2009-05-27 | 青岛高远热能动力设备有限公司 | Multichannel water vapour injector |
| CN101695268A (en) * | 2009-10-30 | 2010-04-21 | 西北农林科技大学 | Pipeline irrigation oxygenation controller |
| EP2208524A1 (en) * | 2002-12-12 | 2010-07-21 | Preseco Oy | Water treatment apparatus comprising dispersion elements for water |
| CN102060256A (en) * | 2010-12-31 | 2011-05-18 | 宋树建 | Pure water filling equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203007003U (en) * | 2012-07-30 | 2013-06-19 | 西藏创源水资源科技有限责任公司 | Nonelectric equipment for producing high-oxygen water |
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2012
- 2012-07-30 CN CN201210264947.4A patent/CN102764605B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1112457A (en) * | 1994-03-15 | 1995-11-29 | 英国氧气集团有限公司 | Gas dissolving |
| US5842600A (en) * | 1996-07-11 | 1998-12-01 | Standex International Corporation | Tankless beverage water carbonation process and apparatus |
| EP2208524A1 (en) * | 2002-12-12 | 2010-07-21 | Preseco Oy | Water treatment apparatus comprising dispersion elements for water |
| CN201244454Y (en) * | 2008-08-20 | 2009-05-27 | 青岛高远热能动力设备有限公司 | Multichannel water vapour injector |
| CN101695268A (en) * | 2009-10-30 | 2010-04-21 | 西北农林科技大学 | Pipeline irrigation oxygenation controller |
| CN102060256A (en) * | 2010-12-31 | 2011-05-18 | 宋树建 | Pure water filling equipment |
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