WO2021003889A1 - Process for preparing high-dissolved oxygen water - Google Patents
Process for preparing high-dissolved oxygen water Download PDFInfo
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- WO2021003889A1 WO2021003889A1 PCT/CN2019/113137 CN2019113137W WO2021003889A1 WO 2021003889 A1 WO2021003889 A1 WO 2021003889A1 CN 2019113137 W CN2019113137 W CN 2019113137W WO 2021003889 A1 WO2021003889 A1 WO 2021003889A1
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- WO
- WIPO (PCT)
- Prior art keywords
- water
- dissolved oxygen
- water source
- high dissolved
- pressure
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 193
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 119
- 239000001301 oxygen Substances 0.000 title claims abstract description 119
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 119
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 230000001954 sterilising effect Effects 0.000 claims abstract description 52
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 52
- 238000001914 filtration Methods 0.000 claims abstract description 31
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 17
- 238000005374 membrane filtration Methods 0.000 claims abstract description 15
- 238000005057 refrigeration Methods 0.000 claims abstract description 12
- 238000013327 media filtration Methods 0.000 claims abstract description 10
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000003756 stirring Methods 0.000 claims description 22
- 238000002360 preparation method Methods 0.000 claims description 16
- 229910001385 heavy metal Inorganic materials 0.000 claims description 8
- 239000012535 impurity Substances 0.000 claims description 8
- 239000012528 membrane Substances 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 7
- 230000004060 metabolic process Effects 0.000 abstract description 5
- 238000000909 electrodialysis Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 235000013619 trace mineral Nutrition 0.000 abstract description 3
- 239000011573 trace mineral Substances 0.000 abstract description 3
- 238000003760 magnetic stirring Methods 0.000 abstract 1
- 238000006213 oxygenation reaction Methods 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
Classifications
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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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- 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
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/22—O2
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
Definitions
- the invention belongs to the technical field of aeration, and particularly relates to a process for preparing high dissolved oxygen water.
- High dissolved oxygen water uses special equipment and technology to purify the oxygen in the air and add it to pure water by physical means to form a solution with higher oxygen content.
- the original high-dissolved oxygen water was dissolved by oxygen for a long time (15-20 hours), which increased the oxygen content in drinking water, and made high-dissolved oxygen water to achieve the purpose of supplementing oxygen through drinking.
- this kind of high dissolved oxygen water has low oxygen content due to the long dissolved oxygen time and simple equipment.
- the oxygen content of high dissolved oxygen water is generally 2-3 times higher than that of natural water, about 20mg/L.
- Traditional methods such as bubbling, spraying, and mechanical stirring and mixing can no longer meet the demand, which greatly limits the preparation of high dissolved oxygen water.
- the oxygen content of high dissolved oxygen water continues to increase, but the oxygen content is still limited.
- many companies have added an electrodialysis process to the water treatment process to make water into pure water. Studies have shown that the water contains a large number of elements and trace elements necessary for human metabolism. However, due to the effect of electrodialysis, these elements are all Being filtered has an indispensable impact on the normal metabolism of the human body.
- the purpose of the present invention is to provide a high-dissolved oxygen water preparation process in view of the shortcomings of the prior art.
- the amount of dissolved oxygen is high, the dissolved oxygen in the water is not volatile, and it will not filter out the large elements and traces necessary for human metabolism. element.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities;
- the low-pressure ultraviolet sterilization is sterilization using low-pressure ultraviolet rays, and the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- the medium-pressure ultraviolet sterilization uses medium-pressure ultraviolet rays for sterilization, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.8 ⁇ -0.2Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high dissolved oxygen water;
- step S1 the precision filtration includes the following operations:
- step S1 the pore size of the ultrafiltration membrane is 0.01-0.1 ⁇ m, the inlet water pressure is 0.1Mpa, and the product water pressure is 0.05 Mpa.
- step S5 the refrigeration treatment maintains the temperature of the water source at 0.1-4.5°C.
- step S6 the water source is passed into the tank at a rate of 1000-10000 mL/min.
- step S6 the stirring speed of the strong magnetic field stirring is 3000-5000 rpm.
- the obtained high dissolved oxygen water has an oxygen content of 25-80 mg/L.
- the present invention provides a process for preparing high dissolved oxygen water, which sequentially passes the water source to be treated through multi-media filtration, precision filtration, ultrafiltration membrane filtration, low-pressure ultraviolet sterilization, magnetization treatment, medium-pressure ultraviolet sterilization and After the refrigeration and other treatment processes, it is then passed into the tank at the same time as the medical oxygen, and fully contacted under the strong magnetic field stirring.
- the oxygen molecules are fully implanted between the water molecules and the water molecules, and the oxygen content is as high as 25-80mg/L. Dissolved oxygen water.
- This application is superior to the application of magnetization treatment to refine the water molecules, and the strong magnetic field stirring makes the oxygen molecules more fully implanted between the water molecules.
- the high dissolved oxygen water dissolved oxygen content obtained by the present invention High, good oxygen-locking effect, the dissolved oxygen in the water is not easy to volatilize, and the present invention does not use electrodialysis and other methods, and will not filter out the large number of elements and trace elements necessary for human metabolism.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities; among them, precision filtration includes the following operations: a) The water source is filtered through a tight filter with a precision of 3 ⁇ m, Filtration pressure ⁇ 0.3Mpa; b) The water source obtained in a) is filtered through a tight filter with a precision of 1 ⁇ m, and the filtration pressure is ⁇ 0.3Mpa; the membrane pore size for ultrafiltration membrane filtration is 0.01 ⁇ 0.1 ⁇ m, and the inlet pressure is 0.1Mpa, production water pressure is 0.05Mpa;
- step S2 performing low-pressure ultraviolet sterilization on the water source obtained in step S1, the low-pressure ultraviolet sterilization uses low-pressure ultraviolet rays for sterilization, the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- step S4 medium-pressure ultraviolet sterilization is performed on the water source obtained in step S3, the medium-pressure ultraviolet sterilization is sterilization by using medium-pressure ultraviolet rays, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4, so that the temperature of the water source is maintained at 0.1°C;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.8Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high-dissolved oxygen water and the water supply rate 1000mL/min, stirring speed 5000rpm;
- S7 Perform ozone sterilization on the primary high dissolved oxygen water obtained in S6 to obtain high dissolved oxygen water with an oxygen content of 80 mg/L.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities; among them, precision filtration includes the following operations: a) The water source is filtered through a tight filter with a precision of 3 ⁇ m, Filtration pressure ⁇ 0.3Mpa; b) The water source obtained in a) is filtered through a tight filter with a precision of 1 ⁇ m, and the filtration pressure is ⁇ 0.3Mpa; the membrane pore size for ultrafiltration membrane filtration is 0.01 ⁇ 0.1 ⁇ m, and the inlet pressure is 0.1Mpa, production water pressure is 0.05Mpa;
- step S2 performing low-pressure ultraviolet sterilization on the water source obtained in step S1, the low-pressure ultraviolet sterilization uses low-pressure ultraviolet rays for sterilization, the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- step S4 medium-pressure ultraviolet sterilization is performed on the water source obtained in step S3, the medium-pressure ultraviolet sterilization is sterilization by using medium-pressure ultraviolet rays, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4, so that the temperature of the water source is maintained at 1°C;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.5Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high-dissolved oxygen water, and the feed rate of the water source 3000mL/min, stirring speed 4500rpm;
- S7 Perform ozone sterilization on the primary high dissolved oxygen water obtained in S6 to obtain high dissolved oxygen water with an oxygen content of 60 mg/L.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities; among them, precision filtration includes the following operations: a) The water source is filtered through a tight filter with a precision of 3 ⁇ m, Filtration pressure ⁇ 0.3Mpa; b) The water source obtained in a) is filtered through a tight filter with a precision of 1 ⁇ m, and the filtration pressure is ⁇ 0.3Mpa; the membrane pore size for ultrafiltration membrane filtration is 0.01 ⁇ 0.1 ⁇ m, and the inlet pressure is 0.1Mpa, production water pressure is 0.05Mpa;
- step S2 performing low-pressure ultraviolet sterilization on the water source obtained in step S1, the low-pressure ultraviolet sterilization uses low-pressure ultraviolet rays for sterilization, the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- step S4 medium-pressure ultraviolet sterilization is performed on the water source obtained in step S3, the medium-pressure ultraviolet sterilization is sterilization by using medium-pressure ultraviolet rays, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4, so that the temperature of the water source is maintained at 2°C;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.4Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high-dissolved oxygen water, and the water supply rate 5000mL/min, stirring speed is 4000rpm;
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities; among them, precision filtration includes the following operations: a) The water source is filtered through a tight filter with a precision of 3 ⁇ m, Filtration pressure ⁇ 0.3Mpa; b) The water source obtained in a) is filtered through a tight filter with a precision of 1 ⁇ m, and the filtration pressure is ⁇ 0.3Mpa; the membrane pore size for ultrafiltration membrane filtration is 0.01 ⁇ 0.1 ⁇ m, and the inlet pressure is 0.1Mpa, production water pressure is 0.05Mpa;
- step S2 performing low-pressure ultraviolet sterilization on the water source obtained in step S1, the low-pressure ultraviolet sterilization uses low-pressure ultraviolet rays for sterilization, the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- step S4 medium-pressure ultraviolet sterilization is performed on the water source obtained in step S3, the medium-pressure ultraviolet sterilization is sterilization by using medium-pressure ultraviolet rays, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4, so that the temperature of the water source is maintained at 3°C;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.3Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high-dissolved oxygen water and the water supply rate 1000 ⁇ 10000mL/min, the stirring speed is 3500rpm;
- S7 Perform ozone sterilization on the primary high dissolved oxygen water obtained in S6 to obtain high dissolved oxygen water with an oxygen content of 25-80 mg/L.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities; among them, precision filtration includes the following operations: a) The water source is filtered through a tight filter with a precision of 3 ⁇ m, Filtration pressure ⁇ 0.3Mpa; b) The water source obtained in a) is filtered through a tight filter with a precision of 1 ⁇ m, and the filtration pressure is ⁇ 0.3Mpa; the membrane pore size for ultrafiltration membrane filtration is 0.01 ⁇ 0.1 ⁇ m, and the inlet pressure is 0.1Mpa, production water pressure is 0.05Mpa;
- step S2 performing low-pressure ultraviolet sterilization on the water source obtained in step S1, the low-pressure ultraviolet sterilization uses low-pressure ultraviolet rays for sterilization, the low-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.01-0.02 MPa;
- step S3 magnetize the water source obtained in step S2 to make the water molecules finer
- step S4 medium-pressure ultraviolet sterilization is performed on the water source obtained in step S3, the medium-pressure ultraviolet sterilization is sterilization by using medium-pressure ultraviolet rays, and the medium-pressure ultraviolet rays, that is, the pressure of the inert gas filled in the lamp is 0.2-0.4 MPa;
- step S5 performing refrigeration treatment on the water source obtained in step S4, so that the temperature of the water source is maintained at 4.5°C;
- step S6 Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.2Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high-dissolved oxygen water and the water supply rate 10000mL/min, stirring speed is 3000rpm;
- S7 Perform ozone sterilization on the primary high dissolved oxygen water obtained in S6 to obtain high dissolved oxygen water with an oxygen content of 25 mg/L.
- a preparation process of high dissolved oxygen water includes the following steps:
- the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities;
- step S2 performing ultraviolet sterilization on the water source obtained in step S1;
- step S3 performing refrigeration treatment on the water source obtained in step S2, so that the temperature of the water source is maintained at 4.5°C;
- step S4 passing the water source and medical oxygen obtained in step S3 into a tank with a vacuum of -0.2 Pa at the same time to obtain primary high dissolved oxygen water;
- the oxygen content of the high dissolved oxygen water in Examples 1 to 5 is higher than that of the high dissolved oxygen water prepared in Comparative Example 1.
- the water source is magnetized to make the water molecules finer.
- a strong magnetic field is used for stirring when the water source is mixed with oxygen, so that the oxygen molecules can be more fully and tightly implanted between the water molecules.
- the present invention also controls the temperature of the water source, the vacuum degree of the tank, the inlet speed of the water source and the stirring speed when the water source is mixed with oxygen.
- the oxygen content of each high dissolved oxygen water will also be different.
- the lower the water temperature, the lower the vacuum degree of the tank, the slower the water inlet speed, the faster the stirring speed, and the higher the dissolved oxygen content within a reasonable range, the lower the water temperature, the lower the vacuum degree of the tank, the slower the water inlet speed, the faster the stirring speed, and the higher the dissolved oxygen content.
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- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
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Abstract
Description
Claims (6)
- 一种高溶氧水制备工艺,其特征在于,包括以下步骤:A preparation process of high dissolved oxygen water is characterized in that it comprises the following steps:S1,将待处理的水源依次经过多介质过滤、精密过滤、超滤膜过滤,去除重金属和杂质;S1, the water source to be treated is sequentially filtered through multi-media filtration, precision filtration, and ultrafiltration membrane filtration to remove heavy metals and impurities;S2,对步骤S1得到的水源进行低压紫外杀菌;S2, performing low-pressure ultraviolet sterilization on the water source obtained in step S1;S3,对步骤S2得到的水源进行磁化处理,使得水分子微细化;S3, magnetize the water source obtained in step S2 to make the water molecules finer;S4,对步骤S3得到的水源进行中压紫外杀菌;S4, performing medium-pressure ultraviolet sterilization on the water source obtained in step S3;S5,对步骤S4得到的水源进行制冷处理;S5, performing refrigeration treatment on the water source obtained in step S4;S6,将步骤S5得到的水源与医用氧同时通入真空度为-0.8~-0.2Pa的罐体中,进行强力磁场搅拌,使得医用氧与水源充分接触,得到初级高溶氧水;S6: Pass the water source and medical oxygen obtained in step S5 into a tank with a vacuum of -0.8~-0.2Pa at the same time, and perform strong magnetic field stirring to make the medical oxygen fully contact the water source to obtain primary high dissolved oxygen water;S7,对S6得到的初级高溶氧水进行臭氧杀菌,得到高溶氧水。S7, ozone sterilization is performed on the primary high dissolved oxygen water obtained in S6 to obtain high dissolved oxygen water.
- 根据权利要求1所述的高溶氧水制备工艺,其特征在于,在步骤S1中,所述精密过滤包括以下操作:The process for preparing high dissolved oxygen water according to claim 1, wherein, in step S1, the precision filtration includes the following operations:a)将水源通入精度为3μm的紧密过滤器进行过滤,过滤压力≤0.3Mpa;a) The water source is filtered with a tight filter with a precision of 3μm, and the filtration pressure is ≤0.3Mpa;b)将a)得到的水源通入精度为1μm的紧密过滤器进行过滤,过滤压力≤0.3Mpa。b) The water source obtained in a) is filtered through a tight filter with a precision of 1 μm, and the filtration pressure is ≤0.3Mpa.
- 根据权利要求1所述的高溶氧水制备工艺,其特征在于,在步骤S1中,所述超滤膜过滤的滤膜孔径为0.01~0.1μm,进水压力为0.1Mpa,产水压力为0.05Mpa。The process for preparing high dissolved oxygen water according to claim 1, wherein in step S1, the pore size of the ultrafiltration membrane is 0.01-0.1 μm, the inlet water pressure is 0.1Mpa, and the product water pressure is 0.05Mpa.
- 根据权利要求1所述的高溶氧水制备工艺,其特征在于:在步骤S5中,所述制冷处理使得水源的温度维持在0.1~4.5℃。The process for preparing high dissolved oxygen water according to claim 1, wherein in step S5, the refrigeration treatment maintains the temperature of the water source at 0.1-4.5°C.
- 根据权利要求1所述的高溶氧水制备工艺,其特征在于:在步骤S6中,所述水源以1000~10000mL/min的速度通入罐体中。The process for preparing high dissolved oxygen water according to claim 1, characterized in that: in step S6, the water source is passed into the tank at a rate of 1000-10000 mL/min.
- 根据权利要求1所述的高溶氧水制备工艺,其特征在于:在步骤S6中,所述强力磁场搅拌的搅拌速度为3000~5000rpm。The process for preparing high dissolved oxygen water according to claim 1, characterized in that: in step S6, the stirring speed of the strong magnetic field stirring is 3000-5000 rpm.根据权利要求1所述的高溶氧水制备工艺,其特征在于:得到的所述高溶氧水的含氧量为25~80mg/L。The process for preparing high dissolved oxygen water according to claim 1, characterized in that the oxygen content of the obtained high dissolved oxygen water is 25-80 mg/L.
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Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020031133A (en) * | 2002-03-18 | 2002-04-26 | 나기선 | Manufacturing method for oxygen condensed water |
CN1473777A (en) * | 2003-07-14 | 2004-02-11 | 吉林市映山红微生物工程有限责任公司 | Process for producing high pressure oxygen ecological water |
CN101654310A (en) * | 2009-08-21 | 2010-02-24 | 厦门西本木式科技有限公司 | Preparation method and device of water containing high dissolved oxygen |
TW201215570A (en) * | 2010-10-01 | 2012-04-16 | Sepoms Technology Co Ltd | Manufacturing method of high dissolved oxygen water and its apparatus |
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 |
CN106315782A (en) * | 2016-09-28 | 2017-01-11 | 连云港利丰医用氧产品有限公司 | Device for producing magnetized high-dissolved-oxygen water |
CN106495375A (en) * | 2016-09-28 | 2017-03-15 | 连云港利丰医用氧产品有限公司 | A kind of preparation method of magnetization water containing high dissolved oxygen |
CN206069477U (en) * | 2016-09-28 | 2017-04-05 | 连云港利丰医用氧产品有限公司 | Magnetization water containing high dissolved oxygen process units |
CN207958041U (en) * | 2017-12-19 | 2018-10-12 | 曾宪群 | The synthesizer of high concentration dissolved oxygen water |
CN110204135A (en) * | 2019-07-05 | 2019-09-06 | 四川神马泉高溶氧集团有限公司 | A kind of water containing high dissolved oxygen preparation process |
-
2019
- 2019-07-05 CN CN201910606261.0A patent/CN110204135A/en active Pending
- 2019-10-24 WO PCT/CN2019/113137 patent/WO2021003889A1/en active Application Filing
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020031133A (en) * | 2002-03-18 | 2002-04-26 | 나기선 | Manufacturing method for oxygen condensed water |
CN1473777A (en) * | 2003-07-14 | 2004-02-11 | 吉林市映山红微生物工程有限责任公司 | Process for producing high pressure oxygen ecological water |
CN101654310A (en) * | 2009-08-21 | 2010-02-24 | 厦门西本木式科技有限公司 | Preparation method and device of water containing high dissolved oxygen |
TW201215570A (en) * | 2010-10-01 | 2012-04-16 | Sepoms Technology Co Ltd | Manufacturing method of high dissolved oxygen water and its apparatus |
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 |
CN106315782A (en) * | 2016-09-28 | 2017-01-11 | 连云港利丰医用氧产品有限公司 | Device for producing magnetized high-dissolved-oxygen water |
CN106495375A (en) * | 2016-09-28 | 2017-03-15 | 连云港利丰医用氧产品有限公司 | A kind of preparation method of magnetization water containing high dissolved oxygen |
CN206069477U (en) * | 2016-09-28 | 2017-04-05 | 连云港利丰医用氧产品有限公司 | Magnetization water containing high dissolved oxygen process units |
CN207958041U (en) * | 2017-12-19 | 2018-10-12 | 曾宪群 | The synthesizer of high concentration dissolved oxygen water |
CN110204135A (en) * | 2019-07-05 | 2019-09-06 | 四川神马泉高溶氧集团有限公司 | A kind of water containing high dissolved oxygen preparation process |
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