CN106219835A - A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic - Google Patents

A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic Download PDF

Info

Publication number
CN106219835A
CN106219835A CN201610823383.1A CN201610823383A CN106219835A CN 106219835 A CN106219835 A CN 106219835A CN 201610823383 A CN201610823383 A CN 201610823383A CN 106219835 A CN106219835 A CN 106219835A
Authority
CN
China
Prior art keywords
water
filter element
filter
core
superfine nano
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610823383.1A
Other languages
Chinese (zh)
Inventor
胡振刚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201610823383.1A priority Critical patent/CN106219835A/en
Publication of CN106219835A publication Critical patent/CN106219835A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00—Clay-wares
    • C04B33/02—Preparing or treating the raw materials individually or as batches
    • C04B33/13—Compounding ingredients
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/02—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by adding chemical blowing agents
    • 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
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic 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
    • C02F1/46—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
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C02F2001/4619—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water only cathodic or alkaline water, e.g. for reducing
    • 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
    • C02F2101/10—Inorganic compounds
    • C02F2101/101—Sulfur compounds
    • 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
    • C02F2101/10—Inorganic compounds
    • C02F2101/12—Halogens or halogen-containing compounds
    • 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
    • C02F2101/10—Inorganic compounds
    • C02F2101/20—Heavy metals or heavy metal compounds
    • 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

Abstract

The invention discloses the manufacturing method and apparatus of the high-purity alkalescent water of a kind of domestic, including: water-making machine shell, size is not more than 60cm 40cm 40cm, inside set PE filter element, activated carbon cartridge, ceramic capillary filter, RO reverse osmosis membrane unit, dissipate carbon core, KDF filter element superfine nano lamination filter element, ion-exchange membrane electrolyzer, water pump and core biomolecule filter element.Present invention employs ultra-fine filter element, permeable membrane is had well protection；The alkalescent water that simple substance molecule ultrafine dust filters after making the electrolysis of film ion achieves high-purity.The present invention reaches 99% to impurity, metal ion, anion, the clearance of sulfur oxynitride, and the filter element of superfine small-bore can carry out ordered arrangement with forces moisture's, forms simple substance small molecule structure, even if at high temperature, also keeps structure constant.The present invention overcomes the difficulty of technique transfers to achieve miniaturization and low cost, especially to old people with suffer from patient for a long time, has more preferably health-care effect.

Description

A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic
Technical field
The present invention relates to water purifier and manufacture the technology of pure water, particularly relate to manufacture the method for high cleanliness drinking water and set Standby.
Background technology
In prior art, in order to obtain pure water, have 200910113006.9, entitled: nano-catalytic light electrolysis The patent of invention of Water warfare decontaminating apparatus and method thereof is applied, and its technical scheme is:
Nano-catalytic micro-electrolytic water purifying and sterilizing device and method thereof are by nano-catalytic light electrolysis machine, sand filtration, three unit of fine straining Constitute.1/20～the 1/5 of the former water purified is needed to enter in nano-catalytic light electrolysis machine, by producing after catalysis and micro-electrolysis Being input to after oxidizing species in neutralizing tank, the former water of remaining 19/20～4/5 is sent directly in neutralization pond urges with nanometer Change micro-electrolytic water mixing makes light electrolysis produce oxidizing species water mix with former water, kill the microorganism in former water, algae, Plankton, and under the effect of electric field, make solid suspension, be dissolved in water colloidal substance, charged particle, algae and quilt Kill antibacterial etc. to form larger particle, after sand filtration is filtered, pump into precise filtering device be filtered to remove；Heavy metal ion in water Cathodic enrichment at light electrolysis forms negative electrode mud precipitation and removes；The Organic substances such as pesticide residues in water, coloring matter, greasy dirt are received The oxidizing species oxidation Decomposition that rice catalysis and micro-electrolysis produces is removed；Phosphate radical in water moves to cathodic polarization layer, with the moon The bivalent cation effect on surface, pole, forms calcium phosphate precipitation and removes.Be widely used in Drinking Water, bitter, sea water and The purified treatment of waste water.
Analyze and research the technical scheme of this patent application, it will thus be seen that one, this technical scheme be a kind of per minute can locate The equipment of the water treatment plant of reason 100kg water, it is impossible to use in the middle of family；Two, this technical scheme only discloses system structure The big parts become, the most concrete technical scheme of each big parts is the openest, from the function of the big system disclosed in it, nothing Method derives the most concrete technical scheme of each big parts.
And make a general survey of the water purifier sold in the market, and mostly using prefilter, the then structure of membrane permeation, it can only Removing impurity and a part of heavy metal ion and anion that in water, granule is bigger, the impurities in water content of output is the most higher, Owing to its technical pattern is simple, although cost is relatively low, but its water quality distance objective value also falls far short.
Therefore, what situation was called can be applicable to family, and cheap, low-profile is compact, can kill many diseases Bacterium virus, purity is not appeared in the newspapers close to the alkalescence water-making machine of desired value.
Summary of the invention
Present invention aims to prior art lacks a kind of that can be applicable to family, cheap, low-profile Compact, many pathogenic bacterias virus can be killed, the deficiency of purity higher alkalescence water-making machine and provide a kind of domestic high-purity The technology of the manufacturing method and apparatus of alkalescent water.
The prefilter of the water-making machine of the present invention have employed ultra-fine filter element, has the permeable membrane of rear class and well protects work With；Simple substance molecule ultrafine dust filtering technique is have employed after membrane permeation, so that the alkalescent water after the electrolysis of film ion Reach high-purity index.
The present invention is by realizing by the following technical solutions.
Implement the manufacture method of the high-purity alkalescent water of a kind of domestic, comprise the steps:
S1, first, arranges a water-making machine shell, and its height is not more than 60cm, and its length is not more than 40cm, and its width is not more than 40cm, is beneficial to install in the family；First one PE filter element is set, is connected on after water inlet switch, in order to filtration of particulate matters Matter, colloidal substance；
S2, then an activated carbon cartridge is set, is connected on after PE filter element, in order to filter free chlorine, hypochlorous acid, carbonate precipitation Thing；
S3, then prepare a ceramic capillary filter, be connected to after activated carbon cartridge, the system of described ceramic capillary filter Make method as follows；
SS31,100kg volcanic rock potter's clay is mixed into 20kg foaming substance；
SS32, add the stirring of 10kg water and become ceramic clay；
SS33, make the briquet of 5 cm 5 cm 5 cm；
SS34, dryness in the sun, make water content 30%；
In SS35, feeding stove, 500 ° of C burn 30 minutes, make to be covered with in briquet the hole of 0.1 m；
SS36, come out of the stove, when temperature is down to 50 ° of C, after kibbling, carry out fine lapping again, be ground to the powdery pottery of diameter 20 m Porcelain raw material, adds the stirring of 2kg water by every 10kg, for pottery wet feed；
SS37, take pottery wet feed and insert in the mould of 2.5cm 5 cm 180cm, with 100kg pressure by the ceramic wet in mould Expect ironed 0.5cm, become the Bulk ceramic filter plate base of 2.0cm 5 cm 180cm；
SS38, Bulk ceramic filter plate base is dried, send in 500 ° of C stoves and fire 30 minutes；
SS39, coming out of the stove is finished product ceramic filtering plate, adds shell encapsulation, is allowed to have current from ceramic filtering plate one side inflow, from separately The structure that side is flowed out；
S4, then after ceramic capillary filter, a RO reverse osmosis membrane unit is set and dechlorinates further and remove microorganism, Connect after described RO reverse osmosis membrane unit and dissipate carbon core, remove abnormal flavour and continuation in water and remove free chlorine；
S5, then connection KDF filter element after scattered carbon core, remove heavy metal and acid ion in water, the ion of protection next stage Exchanger is from chlorine and the pollution of microorganism；
S6 is it follows that connect superfine nano lamination filter element after KDF filter element；The manufacturer of described superfine nano lamination filter element Method is as follows:
SS61, take superfine nano filtering material, with thickness and the size 100kg pressure of 1mm 5cm 180cm, be pressed into For nanofiltration thin slice；
SS62, inserting in mould by 7～10 nanofiltration thin slices, use 100kg pressure, add 120 ° of C temperature, 5 minutes time pressed Make the superfine nano lamination filter element of single sequence arrangement, its pore size filter 10nm～50nm；
S7, then a core biomolecule filter element is set, is connected on after superfine nano lamination filter element, described core biomolecule filter element For remove and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, the tertiary gradient biological harm pathogen and The fourth estate biological harm pathogen；The manufacture method of described core biomolecule filter element is as follows:
SS71, single crystal silicon material is carried out Superfine powder fine grinding, then the granule after fine grinding is carried out the unidirectional selection of molecule, choosing Select aperture standby at the superfine nano silica flour material of 0.01-0.07 micron；
SS72, superfine nano silica flour material is carried out oriented energy process on nuclear magnetic resonance, NMR energy measuring device so that it is become and there is molecule Can the material of unidirectional array performance；
SS73, the superfine nano silica flour material processed is carried out by a certain percentage pulping process: superfine nano silica flour material 40%, water 40%, anhydrous alcohol 20%, then uses 250kg/cm2Pressure depress to the superfine nano silicon embryo of 180mm × 120mm × 10mm Sheet；
SS74, by superfine nano silicon embryo sheet 6500Presintering 1 hour at a temperature of C, then 14000C temperature lower calcination 30 Minute again through 8000Carry out transition cooling at a temperature of C, become superfine nano silicon filter；
SS75, the superfine nano silicon filter firing formation is first carried out cutting edge Shape correction after, pre-packaged in PE Membrane cover；
SS76, PE Membrane cover will not completely enclosed and superfine nano silicon filter therein is embedded in nuclear magnetic resonance apparatus again carrying out The molecule list sequence arrangement of oriented energy processes；
SS77, PE Membrane cover is carried out hermetically sealed formation core biomolecule filter element (18)；
S8 is it follows that arrange an ion-exchange membrane electrolyzer, after being connected on core biomolecule filter element, water carries out soda acid separation, and by Controller detection and control decomposition voltage, obtain alkalescent water；
S9, then export high-purity alkalescent water.
Described controller is also connected with a water pump, before this water pump is arranged on the ceramic capillary filter described in step S3；With It is easy to water and smooth and easy can flow through ceramic capillary filter, RO reverse osmosis membrane unit and superfine nano lamination filter element.
Pressure 8kg～25kg of described water pump.
The porch of the core biomolecule filter element described in step S7, arranges a disjunctor three-way cock,
Two the selection gears closed are used for determining that water is to flow through, be also across core biomolecule filter element.
The detection of described controller and control decomposition voltage, be to measure at the water inlet of ion-exchange membrane electrolyzer
Electrical conductivity, when electrical conductivity is 8～10 s/cm, decomposition voltage is set to 8～10V.
According to the manufacture device of the high-purity alkalescent water of a kind of domestic that said method manufactures and designs, described device includes:
One water-making machine shell, its height is not more than 60cm, and its length is not more than 40cm, and its width is not more than 40cm, is beneficial to be in Front yard is installed；Water-making machine shell is arranged and includes a PE filter element, be connected on after water inlet switch, in order to filter particulate material, colloid Material；
One activated carbon cartridge, is connected on after PE filter element, in order to filter free chlorine, hypochlorous acid, carbonate precipitate；
One ceramic capillary filter, is connected to after activated carbon cartridge；
One RO reverse osmosis membrane unit is connected to after ceramic capillary filter；Connect after described RO reverse osmosis membrane unit and dissipate carbon Core；
Dissipate and connect KDF filter element after carbon core, remove heavy metal and acid ion in water, the ion exchanger of protection next stage from Chlorine and the pollution of microorganism；
Superfine nano lamination filter element is connected after KDF filter element；
One ion-exchange membrane electrolyzer, after being connected on superfine nano lamination filter element, carries out soda acid separation by water, and by controller detection and Control decomposition voltage, obtain alkalescent water.
Described controller is also connected with a water pump, before this water pump is arranged on ceramic capillary filter；So that water can be smooth and easy Flow through ceramic capillary filter, RO reverse osmosis membrane unit and superfine nano lamination filter element.
Pressure 8kg～25kg of described water pump.
After described superfine nano lamination filter element, insert before ion-exchange membrane electrolyzer and a core biomolecule filter element be set, This core biomolecule filter element is used for removing and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, tertiary gradient biology Property harm pathogen and the fourth estate biological harm pathogen；The structure of described core biomolecule filter element is:
The superfine nano silicon filter of 180mm × 120mm × 10mm；Wherein it is covered with the micropore in 0.01-0.07 micron pore size； The molecule list sequence arrangement that described superfine nano silicon filter is oriented energy via nuclear magnetic resonance apparatus is disposed, and carries out with PE Membrane cover Hermetically sealed composition core biomolecule filter element.
In the porch of core biomolecule filter element, arranging a disjunctor three-way cock, two selection gears of this switch are used for Determine that water is to flow through, be also across core biomolecule filter element.
The detection of described controller and control decomposition voltage, be measurement electrical conductivity of water at the water inlet of ion-exchange membrane electrolyzer, When electrical conductivity is 8～10 s/cm, decomposition voltage is set to 8～10V.
Compared with prior art, the manufacturing method and apparatus of the high-purity alkalescent water of the domestic of the present invention realizes technical difficulty Greatly, in order to increase water quality, the difficulty of technique transfers is overcome to be applied among the present invention multiple forward position purification technique, it is achieved that Miniaturization and low cost so that the water generator of the present invention is to impurity, each metal ion species, anion, sulfur oxynitride Clearance reaches 99%, and the filter element of the superfine small-bore of present invention employing can carry out ordered arrangement with forces moisture's, is formed Simple substance small molecule structure, even if under the high temperature conditions, also keeps simple substance small molecule structure constant.
The water manufactured by water purifier sold on the drinking water manufactured by the inventive method, relatively existing market, more to human body Favorably, especially to old people with suffer from patient for a long time, more there is preferable health-care effect.
Accompanying drawing explanation
Below with accompanying drawing, the present invention is further detailed, but the embodiment in accompanying drawing is not constituted this Bright any restriction.
Fig. 1 is the structural representation of the manufacturing method and apparatus of the high-purity alkalescent water of domestic of the present invention.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention will be described.
As it is shown in figure 1, implement the manufacture method of the high-purity alkalescent water of a kind of domestic, comprise the steps:
S1, first, arranges a water-making machine shell 1, and its height is not more than 60cm, and its length is not more than 40cm, and its width is not more than 40cm, is beneficial to install in the family；First one PE filter element 11 is set, is connected on after water inlet switch, in order to filter granule Material, colloidal substance；
S2, then arranging an activated carbon cartridge 12, be connected on after PE filter element 11, in order to filter free chlorine, hypochlorous acid, carbonate sink Shallow lake thing；
S3, then prepare a ceramic capillary filter 13, be connected to after activated carbon cartridge 12, described ceramic capillary filter The manufacture method of 13 is as follows；
SS31,100kg volcanic rock potter's clay is mixed into 20kg foaming substance；
SS32, add the stirring of 10kg water and become ceramic clay；
SS33, make the briquet of 5 cm 5 cm 5 cm；
SS34, dryness in the sun, make water content 30%；
In SS35, feeding stove, 500 ° of C burn 30 minutes, make to be covered with in briquet the hole of 0.1 m；
SS36, come out of the stove, when temperature is down to 50 ° of C, after kibbling, carry out fine lapping again, be ground to the powdery pottery of diameter 20 m Porcelain raw material, adds the stirring of 2kg water by every 10kg, for pottery wet feed；
SS37, take pottery wet feed and insert in the mould of 2.5cm 5 cm 180cm, with 100kg pressure by the ceramic wet in mould Expect ironed 0.5cm, become the Bulk ceramic filter plate base of 2.0cm 5 cm 180cm；
SS38, Bulk ceramic filter plate base is dried, send in 500 ° of C stoves and fire 30 minutes；
SS39, coming out of the stove is finished product ceramic filtering plate, adds shell encapsulation, is allowed to have current from ceramic filtering plate one side inflow, from separately The structure that side is flowed out；
S4, then after ceramic capillary filter 13, a RO reverse osmosis membrane unit 14 is set and dechlorinates further and remove micro- Biology, described RO reverse osmosis membrane unit 14 connects scattered carbon core 15 afterwards, removes abnormal flavour and continuation in water and removes free chlorine；
S5, then connection KDF filter element 16 after scattered carbon core 15, remove heavy metal and acid ion in water, protection next stage Ion exchanger is from chlorine and the pollution of microorganism；
S6 is it follows that connect superfine nano lamination filter element 17 after KDF filter element 16；Described superfine nano lamination filter element 17 Manufacture method is as follows:
SS61, take superfine nano filtering material, with thickness and the size 100kg pressure of 1mm 5 cm 180cm, pressed Become nanofiltration thin slice；
SS62, inserting in mould by 7～10 nanofiltration thin slices, use 100kg pressure, add 120 ° of C temperature, 5 minutes time pressed Make the superfine nano lamination filter element 17 of single sequence arrangement, its pore size filter 10nm～50nm；
S7, then a core biomolecule filter element 18 is set, is connected on after superfine nano lamination filter element 17, described core biomolecule Filter element 18 is used for removing and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, the tertiary gradient biological harm cause of disease Body and the fourth estate biological harm pathogen；The manufacture method of described core biomolecule filter element 18 is as follows:
SS71, single crystal silicon material is carried out Superfine powder fine grinding, then the granule after fine grinding is carried out the unidirectional selection of molecule, Select aperture standby at the superfine nano silica flour material of 0.01-0.07 micron；
SS72, superfine nano silica flour material is carried out oriented energy process on nuclear magnetic resonance, NMR energy measuring device so that it is become and there is molecule Can the material of unidirectional array performance；
SS73, the superfine nano silica flour material processed is carried out by a certain percentage pulping process: superfine nano silica flour material 40%, water 40%, anhydrous alcohol 20%, then uses 250kg/cm2Pressure depress to the superfine nano silicon embryo of 180mm × 120mm × 10mm Sheet；
SS74, by superfine nano silicon embryo sheet 6500Presintering 1 hour at a temperature of C, then 14000C temperature lower calcination 30 Minute again through 8000Carry out transition cooling at a temperature of C, become superfine nano silicon filter；
SS75, the superfine nano silicon filter firing formation is first carried out cutting edge Shape correction after, pre-packaged in PE Membrane cover；
SS76, PE Membrane cover will not completely enclosed and superfine nano silicon filter therein is embedded in nuclear magnetic resonance apparatus again carrying out The molecule list sequence arrangement of oriented energy processes；
SS77, PE Membrane cover is carried out hermetically sealed formation core biomolecule filter element 18；
Water, it follows that arrange an ion-exchange membrane electrolyzer 19, after being connected on core biomolecule filter element 18, is carried out soda acid separation by S8, And detected by controller 20 and control decomposition voltage, obtain alkalescent water；
S9, then export high-purity alkalescent water.
Described controller 20 is also connected with a water pump 21, this water pump 21 be arranged on step S3 ceramic capillary filter 13 it Before；So that water smooth and easy can flow through ceramic capillary filter 13, RO reverse osmosis membrane unit 14 and superfine nano lamination filter element 17.
Pressure 8kg～25kg of described water pump 21.
The porch of the core biomolecule filter element 18 described in step S7, arranges a disjunctor three-way cock 22, the two of this switch Individual selection gear is used for determining that water is to flow through, be also across core biomolecule filter element 18.
Described controller 20 detects and controls decomposition voltage, is the conductance measuring water at the water inlet of ion-exchange membrane electrolyzer 19 Rate, when electrical conductivity is 8～10 s/cm, decomposition voltage is set to 8～10V.
Manufacturing and designing the manufacture device of the high-purity alkalescent water of a kind of domestic, described device includes:
One water-making machine shell 1, its height is not more than 60cm, and its length is not more than 40cm, and its width is not more than 40cm, is beneficial to be in Front yard is installed；Water-making machine shell 1 is arranged and includes a PE filter element 11, be connected on after water inlet switch, in order to filter particulate material, glue Metallic substance；
One activated carbon cartridge 12, is connected on after PE filter element 11, in order to filter free chlorine, hypochlorous acid, carbonate precipitate；
One ceramic capillary filter 13, is connected to after activated carbon cartridge 12；
One RO reverse osmosis membrane unit 14 is connected to after ceramic capillary filter 13；Connect after described RO reverse osmosis membrane unit 14 Connect scattered carbon core 15；
Connect KDF filter element 16 after dissipating carbon core 15, remove heavy metal and acid ion in water, the ion exchanger of protection next stage From chlorine and the pollution of microorganism；
Superfine nano lamination filter element 17 is connected after KDF filter element 16；
One ion-exchange membrane electrolyzer 19, after being connected on superfine nano lamination filter element 17, carries out soda acid separation by water, and by controller 20 Detection and control decomposition voltage, obtain alkalescent water.
Described controller 20 is also connected with a water pump 21, before this water pump 21 is arranged on ceramic capillary filter 13；So that Water smooth and easy can flow through ceramic capillary filter 13, RO reverse osmosis membrane unit 14 and superfine nano lamination filter element 17.
Pressure 8kg～25kg of described water pump 21.
After described superfine nano lamination filter element 17, insert before ion-exchange membrane electrolyzer 19 and a core biomolecule filter is set Core 18, this core biomolecule filter element 18 is used for removing and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, third The biological harm pathogen of level and the fourth estate biological harm pathogen；The structure of described core biomolecule filter element 18 is:
The superfine nano silicon filter of 180mm × 120mm × 10mm；Wherein it is covered with the micropore in 0.01-0.07 micron pore size； The molecule list sequence arrangement that described superfine nano silicon filter is oriented energy via nuclear magnetic resonance apparatus is disposed, and carries out with PE Membrane cover Hermetically sealed composition core biomolecule filter element.
In the porch of core biomolecule filter element 18, a disjunctor three-way cock 22 is set, two selection gears of this switch It is used for determining that water is to flow through, be also across core biomolecule filter element 18.
Described controller 20 detects and controls decomposition voltage, is the conductance measuring water at the water inlet of ion-exchange membrane electrolyzer 19 Rate, when electrical conductivity is 8～10 s/cm, decomposition voltage is set to 8～10V.
Above content is only presently preferred embodiments of the present invention, for those of ordinary skill in the art, according to the present invention's Thought, the most all will change, and this specification content should not be construed as the present invention Restriction.

Claims (10)

1. the manufacture method of the high-purity alkalescent water of domestic, it is characterised in that described method includes step:
S1, first, arranges a water-making machine shell (1), and its height is not more than 60cm, and its length is not more than 40cm, and its width is little In 40cm, it is beneficial to install in the family；One PE filter element (11) is first set, is connected on after water inlet switch, in order to filter Particulate matter, colloidal substance；
S2, then an activated carbon cartridge (12) is set, is connected on after PE filter element (11), in order to filter free chlorine, hypochlorous acid, carbonic acid Root precipitate；
S3, then prepare a ceramic capillary filter (13), be connected to after activated carbon cartridge (12), described ceramic capillary mistake The manufacture method of filter (13) is as follows；
SS31,100kg volcanic rock potter's clay is mixed into 20kg foaming substance；
SS32, add the stirring of 10kg water and become ceramic clay；
SS33, make the briquet of 5 cm 5 cm 5 cm；
SS34, dryness in the sun, make water content 30%；
In SS35, feeding stove, 500 ° of C burn 30 minutes, make to be covered with in briquet the hole of 0.1 m；
SS36, come out of the stove, when temperature is down to 50 ° of C, after kibbling, carry out fine lapping again, be ground to the powdery pottery of diameter 20 m Porcelain raw material, adds the stirring of 2kg water by every 10kg, for pottery wet feed；
SS37, take pottery wet feed and insert in the mould of 2.5cm 5 cm 180cm, with 100kg pressure by the ceramic wet in mould Expect ironed 0.5cm, become the Bulk ceramic filter plate base of 2.0cm 5 cm 180cm；
SS38, Bulk ceramic filter plate base is dried, send in 500 ° of C stoves and fire 30 minutes；
SS39, coming out of the stove is finished product ceramic filtering plate, adds shell encapsulation, is allowed to have current from ceramic filtering plate one side inflow, from separately The structure that side is flowed out；
S4, then after ceramic capillary filter (13), a RO reverse osmosis membrane unit (14) is set and dechlorinates further and go Except microorganism, after described RO reverse osmosis membrane unit (14), connect scattered carbon core (15), remove abnormal flavour in water and dissociate with continuing to remove Chlorine；
S5, then connection KDF filter element (16) after scattered carbon core (15), remove heavy metal and acid ion in water, protect next The ion exchanger of level is from chlorine and the pollution of microorganism；
S6 is it follows that connect superfine nano lamination filter element (17) after KDF filter element (16)；Described superfine nano lamination filter element (17) manufacture method is as follows:
SS61, take superfine nano filtering material, with thickness and the size 100kg pressure of 1mm 5cm 180cm, be pressed into For nanofiltration thin slice；
SS62, inserting in mould by 7～10 nanofiltration thin slices, use 100kg pressure, add 120 ° of C temperature, 5 minutes time pressed Make superfine nano lamination filter element (17) of single sequence arrangement, its pore size filter 10nm～50nm；
S7, then arranging core biomolecule filter element (18), be connected on after superfine nano lamination filter element (17), described core is biological Molecule filter element (18) is used for removing and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, the biological danger of the tertiary gradient Fall ill substance and the fourth estate biological harm pathogen；The manufacture method of described core biomolecule filter element (18) is as follows:
SS71, single crystal silicon material is carried out Superfine powder fine grinding, then the granule after fine grinding is carried out the unidirectional selection of molecule, choosing Select aperture standby at the superfine nano silica flour material of 0.01-0.07 micron；
SS72, superfine nano silica flour material is carried out oriented energy process on nuclear magnetic resonance, NMR energy measuring device so that it is become and there is molecule Can the material of unidirectional array performance；
SS73, the superfine nano silica flour material processed is carried out by a certain percentage pulping process: superfine nano silica flour material 40%, water 40%, anhydrous alcohol 20%, then uses 250kg/cm2Pressure depress to the superfine nano silicon embryo of 180mm × 120mm × 10mm Sheet；
SS74, by superfine nano silicon embryo sheet 6500Presintering 1 hour at a temperature of C, then 14000C temperature lower calcination 30 points Clock is again through 8000Carry out transition cooling at a temperature of C, become superfine nano silicon filter；
SS75, the superfine nano silicon filter firing formation is first carried out cutting edge Shape correction after, pre-packaged in PE Membrane cover；
SS76, PE Membrane cover will not completely enclosed and superfine nano silicon filter therein is embedded in nuclear magnetic resonance apparatus again carrying out The molecule list sequence arrangement of oriented energy processes；
SS77, PE Membrane cover is carried out hermetically sealed formation core biomolecule filter element (18)；
Water, it follows that arrange an ion-exchange membrane electrolyzer (19), after being connected on core biomolecule filter element (18), is carried out soda acid by S8 Separate, and detected by controller (20) and controlled decomposition voltage, obtain alkalescent water；
S9, then export high-purity alkalescent water.
The manufacture method of the high-purity alkalescent water of domestic the most according to claim 1, it is characterised in that:
Described controller (20) is also connected with a water pump (21), and this water pump (21) is arranged on the ceramic capillary filter (13) of step S3 Before；So that water smooth and easy can flow through ceramic capillary filter (13), RO reverse osmosis membrane unit (14) and superfine nano lamination filter Core (17).
The manufacture method of the high-purity alkalescent water of domestic the most according to claim 2, it is characterised in that:
Pressure 8kg～25kg of described water pump (21).
The manufacture method of the high-purity alkalescent water of domestic the most according to claim 1, it is characterised in that: the core described in step S7 The porch of biomolecule filter element (18), arranges a disjunctor three-way cock (22), and two selection gears of this switch are used for determining Water is to flow through, be also across core biomolecule filter element (18).
The manufacture method of the high-purity alkalescent water of domestic the most according to claim 1, it is characterised in that: described controller (20) Detection and control decomposition voltage, be measurement electrical conductivity of water at the water inlet of ion-exchange membrane electrolyzer (19), when electrical conductivity is 8～10 During s/cm, decomposition voltage is set to 8～10V.
6. the manufacture device of the high-purity alkalescent water of domestic, it is characterised in that described equipment includes:
One water-making machine shell (1), its height is not more than 60cm, and its length is not more than 40cm, and its width is not more than 40cm, is beneficial to Family installs；Water-making machine shell (1) is arranged and includes a PE filter element (11), be connected on after water inlet switch, in order to filter granule Material, colloidal substance；
One activated carbon cartridge (12), is connected on after PE filter element (11), in order to filter free chlorine, hypochlorous acid, carbonate precipitate；
One ceramic capillary filter (13), is connected to after activated carbon cartridge (12)；
One RO reverse osmosis membrane unit (14) is connected to after ceramic capillary filter (13)；Described RO reverse osmosis membrane unit (14) Connect afterwards and dissipate carbon core (15)；
Connecting KDF filter element (16) after dissipating carbon core (15), remove heavy metal and acid ion in water, the ion of protection next stage is handed over Parallel operation is from chlorine and the pollution of microorganism；
Superfine nano lamination filter element (17) is connected after KDF filter element (16)；
One ion-exchange membrane electrolyzer (19), after being connected on superfine nano lamination filter element (17), carries out soda acid separation by water, and by controlling Device (20) detects and controls decomposition voltage, obtains alkalescent water.
The manufacture device of the high-purity alkalescent water of domestic the most according to claim 6, it is characterised in that:
Described controller (20) is also connected with a water pump (21), before this water pump (21) is arranged on ceramic capillary filter (13)；Institute State pressure 8kg～25kg of water pump (21), in order to water smooth and easy can flow through ceramic capillary filter (13), RO reverse osmosis membrane unit (14) and superfine nano lamination filter element (17).
The manufacture device of the high-purity alkalescent water of domestic the most according to claim 7, it is characterised in that: at described superfine nano After lamination filter element (17), inserting and arrange core biomolecule filter element (18) before ion-exchange membrane electrolyzer (19), this core biology divides Sub-filter element (18) is used for removing and kill antibiotic medicament in water, alcohol, thin nucleic acid virus, amine, the biological harm of the tertiary gradient Pathogen and the fourth estate biological harm pathogen；In the porch of core biomolecule filter element (18), a disjunctor three is set Opening up pass (22), two of this switch selection gears are used for determining that water is to flow through, be also across core biomolecule filter element (18).
The manufacture device of the high-purity alkalescent water of domestic the most according to claim 6, it is characterised in that: described controller (20) Detection and control decomposition voltage, be measurement electrical conductivity of water at the water inlet of ion-exchange membrane electrolyzer (19), when electrical conductivity is 8～10 During s/cm, decomposition voltage is set to 8～10V.
The manufacture device of the high-purity alkalescent water of domestic the most according to claim 8, it is characterised in that described core biology divides The structure of sub-filter element is:
The superfine nano silicon filter of 180mm × 120mm × 10mm；Wherein it is covered with the micropore in 0.01-0.07 micron pore size； The molecule list sequence arrangement that described superfine nano silicon filter is oriented energy via nuclear magnetic resonance apparatus is disposed, and carries out with PE Membrane cover Hermetically sealed composition core biomolecule filter element.
CN201610823383.1A 2016-09-14 2016-09-14 A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic Pending CN106219835A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610823383.1A CN106219835A (en) 2016-09-14 2016-09-14 A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610823383.1A CN106219835A (en) 2016-09-14 2016-09-14 A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic

Publications (1)

Publication Number Publication Date
CN106219835A true CN106219835A (en) 2016-12-14

Family

ID=58074171

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610823383.1A Pending CN106219835A (en) 2016-09-14 2016-09-14 A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic

Country Status (1)

Country Link
CN (1) CN106219835A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109553226A (en) * 2019-01-15 2019-04-02 天津碧水源膜材料有限公司 Producing water is weakly alkaline nanofiltration water purifier and purifier
CN110407373A (en) * 2018-04-28 2019-11-05 长沙精英军纳米科技有限公司 A kind of preparation process of nanoscale negative hydrogen ion water
CN113277872A (en) * 2021-05-10 2021-08-20 石家庄华行医疗器械有限公司 Vegetarian pottery jar

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101254989A (en) * 2008-02-21 2008-09-03 赖寿全 Device for preparing tea-making water
CN201132805Y (en) * 2007-11-30 2008-10-15 山东益兴实业有限公司 Water-making machine
CN101921029A (en) * 2009-12-21 2010-12-22 张世文 Purification and disinfection device of nano-catalytic micro-electrolytic water and method thereof
CN202146665U (en) * 2011-03-14 2012-02-22 陈贇 Filter element of multi-level filtration water purifier capable of being cleaned
CN102642962A (en) * 2010-11-15 2012-08-22 蔡振生 Production method for alkalescent ionizing and mineralizing drinking water benefiting health
CN103803749A (en) * 2014-02-19 2014-05-21 中治盛业(北京)健康科技有限公司 Preparation method of weak alkaline water for brewing tea
CN206142963U (en) * 2016-09-14 2017-05-03 胡振刚 Domestic high -purity alkalescent water's manufacturing installation

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201132805Y (en) * 2007-11-30 2008-10-15 山东益兴实业有限公司 Water-making machine
CN101254989A (en) * 2008-02-21 2008-09-03 赖寿全 Device for preparing tea-making water
CN101921029A (en) * 2009-12-21 2010-12-22 张世文 Purification and disinfection device of nano-catalytic micro-electrolytic water and method thereof
CN102642962A (en) * 2010-11-15 2012-08-22 蔡振生 Production method for alkalescent ionizing and mineralizing drinking water benefiting health
CN202146665U (en) * 2011-03-14 2012-02-22 陈贇 Filter element of multi-level filtration water purifier capable of being cleaned
CN103803749A (en) * 2014-02-19 2014-05-21 中治盛业(北京)健康科技有限公司 Preparation method of weak alkaline water for brewing tea
CN206142963U (en) * 2016-09-14 2017-05-03 胡振刚 Domestic high -purity alkalescent water's manufacturing installation

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
孙智等: "《材料概论》", 30 November 2008, 中国矿业大学出版社 *
阮国洪: "《水与人类健康》", 31 July 2017, 北京：中国医药科技出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110407373A (en) * 2018-04-28 2019-11-05 长沙精英军纳米科技有限公司 A kind of preparation process of nanoscale negative hydrogen ion water
CN109553226A (en) * 2019-01-15 2019-04-02 天津碧水源膜材料有限公司 Producing water is weakly alkaline nanofiltration water purifier and purifier
CN113277872A (en) * 2021-05-10 2021-08-20 石家庄华行医疗器械有限公司 Vegetarian pottery jar

Similar Documents

Publication Publication Date Title
CN106219835A (en) A kind of manufacturing method and apparatus of the high-purity alkalescent water of domestic
CN102432079B (en) Water purification filter element manufacturing method
Mukhlish et al. Removal of reactive dye from aqueous solution using coagulation–flocculation coupled with adsorption on papaya leaf
KR101780424B1 (en) Apparatus for manufacturing hydrogen water
CN206142963U (en) Domestic high -purity alkalescent water's manufacturing installation
CN104817122A (en) Composite volcanic mineralization filter element and production method thereof
CN215208936U (en) Filter element and single-stage water purifier and multi-stage water purifier applying same
CN201037123Y (en) Highly effective water purifying apparatus
CN107986546B (en) A intensive mixing filters and activation equipment that disinfects for waste water treatment
CN201085965Y (en) Tower equipment for filtering water
CN209161648U (en) A kind of novel casting industry wastewater treatment equipment
CN211688680U (en) Water filter for purifying impure water by magnetic field
CN207347312U (en) Water purifier composite filter element
CN203959983U (en) A kind of nano level filter cartridge construction
CN204897443U (en) Compound volcano rock mineralize mineralization filter core
CN203938557U (en) A kind of novel high magnetic activating water purifier
CN104098167B (en) Dechlorination compositions and Novel filter cartridge
KR101875033B1 (en) Clean water filter with block type water member and water purifying apparatus including the same
CN205635232U (en) Purifier is strained to nanometer no. 3
CN205170525U (en) Special strainer of scenic water
CN206915880U (en) A kind of Novel water purifier filter element
CN204265573U (en) A kind of high strontium natural mineral water purification system
CN108996748A (en) A kind of novel casting industry wastewater treatment equipment
CN204752360U (en) Filter water purifier of crossing of running water chlorine residue
CN107285735A (en) A kind of ceramic water filter filter core and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20161214

WD01 Invention patent application deemed withdrawn after publication