CN1067660C - Production of rich oxygen content drinking water - Google Patents
Production of rich oxygen content drinking water Download PDFInfo
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- CN1067660C CN1067660C CN 95108667 CN95108667A CN1067660C CN 1067660 C CN1067660 C CN 1067660C CN 95108667 CN95108667 CN 95108667 CN 95108667 A CN95108667 A CN 95108667A CN 1067660 C CN1067660 C CN 1067660C
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- water
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- reverse osmosis
- tap water
- filtration
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Abstract
The present invention discloses a method for preparing drinking water with high oxygen content. The method of the present invention is characterized in that water orderly flows through a raw water inlet device, a filter, a water softening device, a deodorizing device, a filter membrane device, a water collecting and reacting device, an ozone sterilizing device, a fine filter, a liquefied oxygen supplier and a water supply device.
Description
The present invention relates to a kind of manufacture method of rich oxygen content drinking water, further say, the manufacture method of the rich oxygen content drinking water that particularly a kind of complete drinking-water quality is handled.
Water is requisite indispensable among the human lives really, takes a broad view of over one, more than two decades, takes off and is close to the gold period that reaches summit in climbing on the occasion of international economy, is accompanied by this prime time also to have brought up the material progress of height simultaneously.And in this period, the mankind almost enjoy the contour nutritional amt food of plenty of meat and fish everyday, or enjoy human body hundred none beneficial junk foods everyday; Especially bad, human aspect beverage selects for use in this period, more almost to give up and drink boiled water and select sugar degree high or high-octane cola, carbonated drink or sports beverages for use, aforementioned food and beverage are selected for use for a long time, bring up the fat youngster of many mistakes really; Moreover the selecting for use for a long time of aforementioned food and beverage, the human beings'health situation but presents the fact that go fromes bad to worse, and such as generally suffering from of ciril diseases such as hematologic disease, hypertension or vascular lesion, really also makes us shocking!
In view of this, also common human many salt-free diets of advocating in the recent period, do more physical exercises, drink actual property and significant slogan and action such as boiling water more, yet just the mankind do one's utmost to advocate drink boiling water more in, find in the stage of more preceding economic take-offs also simultaneously, environment and water source have been paid also by the heavy cost of severe contamination, the water quality extreme difference that causes some areas tap water, difference to regional local-style dwelling houses perhaps only wash with tap water, the pouring and dare not be as drinking, the water of drinking but from or buy and to identify oneself mountain spring water or the mineral water that tool not pollutes, this phenomenon is really also very sad for satirizing! So with regard to mountain spring water or mineral water, the place, water source was perhaps not contaminated really, but with regard to health, sterilization and to remove the processing of items such as harmful material really really obviously not enough, it may not process fully, also may only do easy sterilization or filtration treatment and peddle at once for the human consumer and use.Custom meaning " illness finds its way in by the mouth ", for accounting for the human body weight percentage water of usage quantity maximum when, can be not careful!
Present commercially available fountain water or mineral water, its water source perhaps is upstream, water source or the mountain area that is taken from without polluting, right with regard to the theory of tap water, no matter drinking water source is where to be taken from, do suitable processing if in the treatment scheme of indispensabilities such as sterilization, filtering water, cooperate necessaries in fact, no matter be the water source that is taken from Anywhere then, should completely be processed into the healthy water or the so-called pure water that are beneficial to use most, think that Ying Kezai more researches and develops improvement and these treating processess are the applicant, the water quality of tap water can more be progressed greatly.
Main purpose of the present invention promptly is to provide the manufacture method of the rich oxygen content drinking water that a kind of complete drinking water quality handles, to improve the water quality of tap water.
For achieving the above object, method provided by the invention is characterised in that passes through water in regular turn by former water water feed apparatus, filtration unit, demineralized water treatment device, odor removal, filtration film device, the reaction unit that catchments, ozone sterilization device, the secondary filter device, water supply installation, the producing apparatus of the rich oxygen content drinking water that a kind of complete drinking-water quality that the liquid oxygen feeding mechanism combines is handled, and can provide tap water best in quality according to various demand mode; Simultaneously, the present invention also can be provided with the accurate reverse osmosis membrane device of removing organism, inorganics or harmful element of an energy between odor removal and filtration film device.
The flow process of present method is to comprise in regular turn passes through water as lower device:
Former water water feed apparatus, it is the container at a splendid attire water source;
Filtration unit, it is arranged in after the former water water feed apparatus, and portion is filled with the filter material of quartz sand or manganese sand within it, to filter mud matter in the tap water, calcium carbonate, irony and to the disadvantageous heavy metal of tap water in advance;
Demineralized water treatment device, it is arranged in after the aforementioned filtration unit, and portion is filled with resin with demineralized water within it;
Odor removal, it is arranged in after the aforementioned demineralized water treatment device, and portion is filled with gac to remove stink within it;
Filtration film device, it is arranged in after the aforementioned odor removal, and the aperture wherein is housed is that the filtering membrane of 10-200 dust is to remove the organism in the tap water;
The reaction unit that catchments, it is arranged in the tap water that is used for concentrating after the aforementioned filtration film device through pre-process, and its internal temperature is 0-30 ℃;
The ozone sterilization device, it comprises power supply, ozonizer and quantitative controller, and links to each other so that will be poured into the aforementioned reaction unit inside of catchmenting by the ozone that ozonizer produces quantitatively with the aforementioned reaction unit that catchments;
The secondary filter device, it is arranged in after the aforementioned reaction unit that catchments, and to have the aperture be that the filtering membrane of 100 dusts is to do the filtration before supplying water again;
The liquid oxygen feeding mechanism, it is arranged in aforementioned secondary filter device afterwards to improve the oxygen level of tap water;
Water supply installation, it is arranged in after the aforementioned liquid oxygen feeding mechanism so that supply water according to various demand mode.
In another embodiment of the invention, also can be provided with the reverse osmosis membrane device between odor removal and filtration film device, this reverse osmosis membrane device comprises the backflow water pipe that is positioned at centre, the reverse osmosis supporting layer that is distributed in the periphery and the reverse osmosis rete that is positioned at reverse osmosis membrane supporting layer inboard.
Below by preferred embodiment and conjunction with figs. the manufacture method of rich oxygen content drinking water of the present invention is done more detailed description, in the accompanying drawings:
Fig. 1 is the producing apparatus schema of one embodiment of the invention,
Fig. 2 is the organigram of ozone sterilization device of the present invention,
Fig. 3 is the producing apparatus schema of another embodiment of the present invention,
Fig. 4 is the schematic perspective view of permeable membrane device of the present invention.
As shown in Figure 1, it is one of embodiment of the invention manufacture method schema, and the present invention mainly includes in regular turn as seen from the figure: former water water feed apparatus 10, but it is the container at a splendid attire such as water sources such as river, stream underground water; Filtration unit 11, be to be arranged in after the former water water feed apparatus 10 and can to utilize its inner filter material of filling to filter bad thing in the tap water in advance, as mud matter, calcium carbonate, irony or other heavy metals, wherein the filter material of this filtration unit 11 can be and can remove mud matter or calcareous quartz sand 110, or for removing manganese sand 111 as heavy metal such as arsenic, cadmium, mercury, lead, silver or irony, and or the two use simultaneously; Demineralized water treatment device 12 is to be arranged in aforementioned filtration unit 11 can utilize its inner material demineralized water of filling afterwards, the material class such as the resin of this type of demineralized water treatment device 12, and it can make the hard water of tap water by the puckery perceptual matter of flavor tool, changes over the soft water of the smooth sense of flavor tool; Odor removal 13 is to be arranged in aforementioned demineralized water treatment device 12 can utilize its inner material of filling to remove stink afterwards, the material class such as the activated carbon of this type of odor removal 13, and it has the function of deodorant to taste; Filtration film device 14, be to be arranged in after the aforementioned odor removal 13 and can to utilize the fine pore size of its filtering membrane to remove organism in the tap water, or as the subtitle substance of tea stain and so on, this filtration film device 14 is can be as ultrafilter membrane device (ULTRAFILTRATION), and the aperture of its filtering membrane is about the 10-200 dust; The reaction unit 15 that catchments is to be arranged in after the aforementioned filtration film device 14 and can to concentrate the tap water that passes through pre-process; Ozone sterilization device 16, be but that quantitative perfusion ozone is in the tap water of aforementioned reaction unit 15 inside of catchmenting, so that the ozone that dissolves in the tap water can fully continue sterilization in follow-up retardation is handled the period, the volatility of ozone is extremely strong and can be quickly dissolved in the water and become the oxygen state, it has good sterilization effect and can promote the rich oxygen content of drinking, the general water-soluble rate of ozone when lesser temps is bigger, so if can cooperate reaction unit 15 internal temperatures that catchment to be in 0-30 ℃ the scope for best; Secondary filter device 17, be to be arranged in the aforementioned reaction unit 15 that catchments to utilize the fine pore size of its filtering material to do the preceding filtration of supplying water again afterwards, the filtering material of this secondary filter device 17 can adopt the filtering material as stainless steel or film-type corrosion stability to be the best, and the aperture is about 100 dusts; Liquid oxygen feeding mechanism 18 is to be arranged in the oxygen level that aforementioned secondary filter device 17 can improve tap water afterwards, promotes the metabolic effect of the new battle array of human body; Water supply installation 19 is to be arranged in aforementioned liquid oxygen feeding mechanism 18 to supply water according to various demand mode afterwards, and certainly, the present invention also can be provided with aqua storage tank (part dotted line finger part of living in as figure) according to need in the appropriate location of integral device.
The structure of aforementioned ozone sterilization device 16 roughly as shown in Figure 2, it mainly is that mat power supply 160 makes the oxygen that enters ozone generation device 161 resolve into ozone as seen from the figure, and can ozone quantitatively be input into the rich oxygen content that catchments reaction unit 15 inside and be dissolved in the water and produce good sterilization effect and can promote tap water via quantitative controller 162.
As shown in Figure 3, it is the manufacture method schema of another embodiment of the present invention, the device of this embodiment still roughly is same as aforementioned as seen from the figure, that is it still includes former water water feed apparatus in regular turn, filtration unit, demineralized water treatment device, odor removal, filtration film device, the reaction unit that catchments, ozone sterilization device, the secondary filter device, the liquid oxygen feeding mechanism, structures such as water supply installation only are as for the difference place of this embodiment and last embodiment, this embodiment can be provided with one between odor removal 23 and filtration film device 24 can accurately remove organism, the reverse osmosis membrane device 27 of inorganics or harmful element, also be provided with the reaction unit 25 that catchments after filtration film device 24 in regular turn, ozone sterilization device 26 sees also schematic perspective view shown in Figure 4 as for the structure of reverse osmosis membrane device 27.Reverse osmosis membrane device 27 consists predominantly of the backflow water pipe 270 that is in centre as seen from the figure, be distributed in peripheral reverse osmosis membrane supporting layer 271, and the contrary rete 272 that oozes that is positioned at reverse osmosis membrane supporting layer 271 inboards, make via pre-process tap water later after water inlet enters permeable membrane device 27, promptly divide and be between the reverse osmosis membrane layer 272, gradually be removed organism, inorganics or harmful element, just flow out via outlet afterwards, as for still fail the water of complete processing then can be again reflux by backflow water pipe 270 after again recirculation handle,, will no longer be described in detail because of can frequently seeing the market based on the structure of reverse osmosis membrane device 27 in this.
The manufacture method of rich oxygen content drinking water of the present invention, simple, purification of water quality is thorough, oxygen level is high.
Claims (2)
1, a kind of manufacture method of tap water is characterized in that in regular turn water being passed through as lower device:
Former water water feed apparatus, it is the container at a splendid attire water source;
Filtration unit, it is arranged in after the former water water feed apparatus, and portion is filled with the filter material of quartz sand or manganese sand within it, to filter mud matter in the tap water, calcium carbonate, irony and to the disadvantageous heavy metal of tap water in advance;
Demineralized water treatment device, it is arranged in after the aforementioned filtration unit, and portion is filled with resin with demineralized water within it;
Odor removal, it is arranged in after the aforementioned demineralized water treatment device, and portion is filled with gac to remove stink within it;
Filtration film device, it is arranged in after the aforementioned odor removal, and the aperture wherein is housed is that the filtering membrane of 10-200 dust is to remove the organism in the tap water;
The reaction unit that catchments, it is arranged in the tap water that is used for concentrating after the aforementioned filtration film device through pre-process, and its internal temperature is 0-30 ℃;
The ozone sterilization device, it comprises power supply, ozonizer and quantitative controller, and links to each other so that will be poured into the aforementioned reaction unit inside of catchmenting by the ozone that ozonizer produces quantitatively with the aforementioned reaction unit that catchments;
The secondary filter device, it is arranged in after the aforementioned reaction unit that catchments, and to have the aperture be that the filtering membrane of 100 dusts is to do the filtration before supplying water again;
The liquid oxygen feeding mechanism, it is arranged in aforementioned secondary filter device afterwards to improve the oxygen level of tap water;
Water supply installation, it is arranged in after the aforementioned liquid oxygen feeding mechanism so that supply water according to various demand mode.
2, manufacture method as claimed in claim 1, wherein be provided with the reverse osmosis membrane device between odor removal and filtration film device, this reverse osmosis membrane device comprises the backflow water pipe that is positioned at centre, the reverse osmosis supporting layer that is distributed in the periphery and the reverse osmosis rete that is positioned at reverse osmosis membrane supporting layer inboard.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95108667 CN1067660C (en) | 1995-08-04 | 1995-08-04 | Production of rich oxygen content drinking water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95108667 CN1067660C (en) | 1995-08-04 | 1995-08-04 | Production of rich oxygen content drinking water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1142468A CN1142468A (en) | 1997-02-12 |
| CN1067660C true CN1067660C (en) | 2001-06-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95108667 Expired - Fee Related CN1067660C (en) | 1995-08-04 | 1995-08-04 | Production of rich oxygen content drinking water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1067660C (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102020386A (en) * | 2010-12-09 | 2011-04-20 | 浙江米利空气制水科技有限公司 | Multifunctional drinking water producing equipment and water treatment process |
| CN104944652A (en) * | 2015-06-09 | 2015-09-30 | 甘肃京奥港天然矿泉饮品有限公司 | Oxygen-rich water production process |
| CN105174543A (en) * | 2015-09-21 | 2015-12-23 | 海南仙都峰科技有限公司 | Direct drinking water purifying method and device |
| CN106587457A (en) * | 2016-11-14 | 2017-04-26 | 无锡艾科瑞思产品设计与研究有限公司 | Purification and detection supplying equipment of tap water |
-
1995
- 1995-08-04 CN CN 95108667 patent/CN1067660C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN1142468A (en) | 1997-02-12 |
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